LAND-BASED ALGAL MARICULTURE FOR OCEAN DEACIDIFICATION All documents cited herein are incorporated by reference in their entirety. TECHNICAL FIELD The present invention relates to methods for ocean deacidification by culturing algae in land-based mariculture and to methods for carbon sequestration by culturing algae in land-based mariculture. BACKGROUND According to a 2017 report by the UK Government Office for Science, mean global surface ocean pH has decreased from 8.2 to 8.1, the equivalent of a 25% increase in hydrogen ion concentration. A 2018 report by the Ocean Acidification subgroup of the UK Science Advisory Council states that, under the carbon emission commitments under the Paris Agreement, there will be a further decrease of 0.2-0.3 units by 2100, or 0.4 units if carbon emissions continue at their current levels. Ocean acidification will have profound, global effects on wildlife, food supply, coastal protection and tourism. For example, the shells of marine molluscs will become less dense and weaker, which will in turn affect populations and communities who depend upon seafood as a key source of nourishment. There is a pressing need for new, innovative strategies which proactively tackle decreasing ocean pH alongside steps to reduce our ever-increasing levels of carbon emissions. SUMMARY OF THE INVENTION The inventors have devised a new method for ocean deacidification that involves culturing algae in land-based mariculture. The method comprises three phases: a first algal culture phase, a second algal culture phase, and a discharge phase. During the first algal culture phase, one or more nutrient mineral acids are added, with the surprising effect of resulting in an overall increase in the pH achieved by the end of the second algal culture phase. This enhances the ocean de-acidification that results from the algal culture discharge water being discharged into the ocean. In addition, supplementation with nutrient mineral acids in the first algal culture phase results in highly efficient removal of dissolved inorganic carbon (DIC) from the mariculture, which advantageously translates into an improved rate of algal biomass production. Accordingly, the invention provides a method for ocean deacidification, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4 and (c) a discharge phase, wherein the discharge phase comprises discharging de-acidified water obtained from step (b) into the ocean. In some embodiments, the one or more nutrient mineral acids are selected from nitric acid, phosphoric acid and silicic acid. In some embodiments, step (a) further comprises monitoring the pH of the land-based mariculture (e.g. with a pH sensor). In some embodiments, the discharging of de-acidified water comprises the use of one or more discharge channels that have a width to depth ratio of greater than 50:1. In some embodiments, the one or more discharge channels are more than 2 km long. In some embodiments, the discharge water entering the ocean is at least 0.1 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at least 0.2 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at least 0.3 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at least 0.5 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is 0.1-1.2 pH units (e.g.0.1-0.5 pH units) higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is 0.1-0.3 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at pH 8.2-9.0. In some embodiments, the discharge water entering the ocean is at pH 8.2-8.8. In some embodiments, the discharge water entering the ocean is at pH 8.3-8.6. In some embodiments, the land-based mariculture in steps (a) and (b) comprises one or more raceway ponds. In some embodiments, the land-based mariculture in step (a) comprises culturing the algae in a series of connected raceway ponds, arranged in stages. In some embodiments, the series of connected raceway ponds comprises a first stage comprising one or more covered raceway ponds and a second stage comprising one or more stages of open raceway ponds. In some embodiments, the land-based mariculture in step (b) comprises culturing the algae in a raceway pond, wherein the raceway pond is connected to the series of connected raceway ponds in which algae are cultured in step (a). In some embodiments, the method further comprises harvesting the algae before performance of step (c). In some such embodiments, the method further comprises burying the harvested algae for carbon sequestration. In some such embodiments, a slurry or a concentrate of the harvested algae is solar dried prior to burial. In some embodiments, the algae are: (i) bloom-forming microalgae or diatoms that have the ability to grow exponentially or with a cell division rate exceed one division per day, (ii) diazotrophic phytoplankton and/or (iii) diatom-diazotroph assemblages (DDAs). In some embodiments, the bloom-forming microalgae and diazotrophic phytoplankton are cyanobacteria. In some embodiments, the bloom-forming microalgae and diazotrophic phytoplankton is Trichodesmium sp. In some embodiments, the bloom-forming microalgae, diazotrophic phytoplankton and/or DDAs comprise: (i) one or more of the following diazotrophs: Richelia sp., Calothrix sp., Crocosphaera sp. and Candidatus Atelocynaobacterium Thalassa, and/or (ii) one or more of the following diatoms: Hemiaulus sp. and Climacodium sp. (iii) one or more of the following: Skeletonema spp., Chaetoceros spp., Thalassiosira spp., Coscinodiscus spp., Navicula spp., Synedra sp. and Nitzschia spp., or (iv) Dunaliella spp. In some embodiments, the DDAs comprise Hemiaulus sp. (e.g. an assemblage of Richelia sp. and Hemiaulus sp.). The inventors have further have devised a new method for sequestering carbon dioxide. In this method, carbon dioxide is sequestered by the algae during culture. In addition, the de-acidified water discharged from the algal culture absorbs carbon dioxide while flowing through discharge channels to the ocean. In general, the surface area of the discharge water-air interface in the discharge channels is large enough that carbon dioxide absorption by the discharge water occurs to the extent that the high pH of the discharge water decreases to approximately the pH level of the ocean. The invention further provides a method for sequestering carbon dioxide from the atmosphere, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4, wherein the discharge water-air interface has a surface area that is at least 1 km ² , wherein the discharge water entering the ocean is at a pH that is no more than 0.3 pH units higher than the pH of the ocean, and (c) a discharge phase, wherein the discharge phase comprises discharging de-acidified water obtained from step (b) into the ocean. In some embodiments, the discharge water-air interface has a surface area that is at least 2 km ² . In some embodiments, the discharge water-air interface has a surface area that is at least 5 km ² . In some embodiments, the discharge water-air interface has a surface area that is at least 10 km ² . In some embodiments, the discharge water-air interface has a surface area that is 5-10 km ² . In some embodiments, each of the one or more discharge channels has a volume of at least one million cubic metres. In some embodiments, each of the one or more discharge channels has a volume of at least 2.5 million cubic metres. In some embodiments, each of the one or more discharge channels has a volume of 1-5 million cubic metres. In some embodiments, each of the one or more discharge channels has a length of at least 10 km, at least 25 km, at least 50km or at least 100 km. In some embodiments, each of the one or more discharge channels has a width of 25-250 m (e.g. 50-100 m). In some embodiments, each of the one or more discharge channels has a depth of 0.1-5 m. In some embodiments, each of the one or more discharge channels has a depth of 0.25-1 m. In some embodiments, each of the one or more discharge channels has a depth of 0.4-0.6 m. In some embodiments, the discharge water entering the ocean is at a pH that is no more than 0.2 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at a pH that is no more than 0.1 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at a pH that is the same as the pH of the ocean. In some embodiments, the discharge water entering the ocean is pH 8.4 or lower. In some embodiments, the discharge water entering the ocean is at pH 8.0-8.4 (e.g. pH 8.0-8.2). The invention further provides algae obtained by a method of the invention. BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 illustrates an example raceway pond according to the invention. Figure 2A illustrates an algal cultivation system depicts a series of connected raceway ponds arranged in stages according to the invention. Figure 2B illustrates a subsection of the algal cultivation system of Figure 2A. Figure 3: A raceway pond with two channels. Features include an inlet pipe, a paddle wheel, flow diverters, a drain pipe, side walls and dividers. The side walls and dividers may be formed of plastic covered and reinforced walls or berms. The paddlewheel is typically a variable speed paddlewheel. The flow diverters act to maintain laminar flow. The inlet pipe may be connected to a gate-controlled sluice for pond intake from either a seawater canal and/or the previous ponds. The drain pipe facilitates pond discharge through a gate controlled sluice. Figure 4: a series of connected raceway ponds arranged in stages. The schematic outlines: • Intake pipeline • Elevated supply canal filled from intake pipeline with high-rate, low-head pumps • Greenhouse-covered sequential seed ponds filled with filtered seawater to grow inoculum for growth ponds • Uncovered, sequential growth ponds connected with and filled from previous pond plus fresh seawater from supply canal • Harvesting ponds for grow-out before harvesting • Harvesting canal and harvesting building • Low elevation discharge pipeline Figure 5: Comparison of the effects of nutrient acid supplementation, nutrient supplementation and no supplementation on pH in pond seawater. Figure 6: Comparison of the effects of nutrient acid supplementation, nutrient supplementation and no supplementation on dissolved inorganic carbon levels in pond seawater. DETAILED DESCRIPTION OF THE INVENTION Nutrient mineral acids As used herein, “nutrient mineral acid” refers to an inorganic acid in which the conjugate base provides nourishment for algae (e.g. the conjugate base is used by algae to survive and grow). In the invention, one or more nutrient mineral acids are added in the first algal culture phase. In some embodiments, the one or more nutrient mineral acids are selected from a phosphorus-containing acid, silicon-containing acid, nitrogen-containing acid. In some embodiments, a phosphorus-containing acid is added in the first algal culture phase. In general, all algae assimilate phosphorus for survival and growth. Therefore, phosphorus-containing acids are nutritious for any algal species. In some embodiments, the nutrient mineral acid is a phosphorus oxoacid. In some embodiments, the nutrient mineral acid has a phosphate anion as a conjugate base. In some embodiments, the nutrient mineral acid is a phosphoric acid. In some embodiments, the phosphoric acid has the chemical formula H ₃ PO ₄ . In preferred embodiments, the phosphorus-containing acid is phosphoric acid (H ₃ PO ₄ ) In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final concentration of at least 0.15 μM, at least 0.5 μM, at least 1.0 μM, at least 1.5 μM, at least 2.0 μM, at least 5.0 μM, at least 10 μM, or at least 15 μM. In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final concentration of 0.15-15 μM (e.g. 0.5-4.5 μM, such as 1-2 μM). In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final concentration of between 0.1 μM and 2.0 μM, between 0.5 μM and 2.0 μM, or between 1.0 μM and 2.0 μM. In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final concentration of 1.5 μM. The concentration of phosphorus-containing acid that is added can be influenced by the algal cell density. Accordingly, in some embodiments, phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 5 to (ii) number of thousand algal cells per ml multiplied by 25. In some embodiments, phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 7 to (ii) the number of thousand algal cells per ml multiplied by 15. In some embodiments, phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 10 to (ii) the number of thousand algal cells per ml multiplied by 13. In some embodiments, phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 5. In some embodiments, phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 10. In some embodiments, phosphorus- containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 12. In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 15. In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 20. In some embodiments, phosphorus- containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 25. In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 5. In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 10. In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 12. In some embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 15. In some embodiments, phosphorus- containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 20. In some embodiments, phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 25. In some embodiments, the phosphorous-containing conjugate base to the phosphorous-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final concentration of at least 0.15 μM, at least 0.5 μM, at least 1.0 μM, at least 1.5 μM, at least 2.0 μM, at least 5.0 μM, at least 10 μM, or at least 15 μM. In some embodiments, the phosphorous-containing conjugate base to the phosphorous-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final concentration of 0.15-15 μM (e.g. 0.5-4.5 μM, such as 1-2 μM). In some embodiments, the phosphorous-containing conjugate base to the phosphorous-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final concentration of between 0.1 μM and 2.0 μM, between 0.5 μM and 2.0 μM, or between 1.0 μM and 2.0 μM. In some embodiments, the phosphorous-containing conjugate base to the phosphorous-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final concentration of 1.5 μM. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 5 to (ii) number of thousand algal cells per ml multiplied by 25. In some embodiments, the phosphorous- containing conjugate base to the phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 7 to (ii) the number of thousand algal cells per ml multiplied by 15. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 10 to (ii) the number of thousand algal cells per ml multiplied by 13. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 5. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 10. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 12. In some embodiments, the phosphorous- containing conjugate base to the phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 15. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 20. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 25. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 5. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 10. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H3PO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 12. In some embodiments, the phosphorous-containing conjugate base to the phosphorus- containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 15. In some embodiments, the phosphorous-containing conjugate base to the phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 20. In some embodiments, the phosphorous- containing conjugate base to the phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 25. In some embodiments, phosphorous is added in the first algal culture phase to a final concentration of at least 0.15 μM, at least 0.5 μM, at least 1.0 μM, at least 1.5 μM, at least 2.0 μM, at least 5.0 μM, at least 10 μM, or at least 15 μM. In some embodiments, phosphorous is is added in the first algal culture phase to a final concentration of 0.15-15 μM (e.g. 0.5-4.5 μM, such as 1-2 μM). In some embodiments, phosphorous is added in the first algal culture phase to a final concentration of between 0.1 μM and 2.0 μM, between 0.5 μM and 2.0 μM, or between 1.0 μM and 2.0 μM. In some embodiments, phosphorous is added in the first algal culture phase to a final concentration of 1.5 μM. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 5 to (ii) number of thousand algal cells per ml multiplied by 25. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 7 to (ii) the number of thousand algal cells per ml multiplied by 15. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 10 to (ii) the number of thousand algal cells per ml multiplied by 13. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 5. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 10. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 12. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 15. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 20. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 25. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 5. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 10. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 12. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 15. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 20. In some embodiments, phosphorus is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 25. In some embodiments, a silicon-containing acid is added in the first algal culture phase. Some algal species (e.g. diatoms) assimilate silicon as a component of their cell walls. Therefore, silicon-containing acids are nutritious for algal species with silica cell wells (e.g. diatoms). In some embodiments, the nutrient mineral acid has a silicate anion as a conjugate base. In some embodiments, the nutrient mineral acid is a silicic acid. In some embodiments, the nutrient mineral acid is orthosilicic acid, metasilicic acid, pyrosilicic acid or disilicic acid. In preferred embodiments, the silicon-containing acid is orthosilicic acid (H4SiO4). In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final concentration of at least 0.3 μM, at least 0.5 μM, at least 1.0 μM, at least 1.5 μM, at least 2.0 μM, at least 5.0 μM, at least 10 μM, at least 15 μM, or at least 30 μM. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final concentration of 0.3-30 μM (e.g. 1-9 μM, such as 2-4 μM). In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final concentration of between 0.3 μM and 5.0 μM, between 0.5 μM and 5 μM, between 1.0 μM and 5.0 μM, between 1.5 μM and 5.0 μM, between 2.0 μM and 5.0 μM, between 2.5 μM and 5.0 μM, between 2.5 μM and 4.5 μM, between 2.5 μM and 4.0 μM or between 2.5 μM and 3.5 μM. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final concentration of 3 μM. The concentration of silicon-containing acid (e.g. H ₄ SiO ₄ ) that is added can be influenced by the algal cell density. Accordingly, in some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 5 to (ii) number of thousand algal cells per ml multiplied by 50. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 15 to (ii) the number of thousand algal cells per ml multiplied by 35. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 20 to (ii) the number of thousand algal cells per ml multiplied by 30. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 22 to (ii) the number of thousand algal cells per ml multiplied by 26. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 5. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 10. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 15. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 20. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 25. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 30. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 40. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 50. In some embodiments, silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 5. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 10. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 15. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 20. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 25. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 30. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 40. In some embodiments, silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 50. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final concentration of at least 0.15 μM, at least 0.5 μM, at least 1.0 μM, at least 1.5 μM, at least 2.0 μM, at least 5.0 μM, at least 10 μM, or at least 15 μM. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final concentration of 0.15-15 μM (e.g.0.5- 4.5 μM, such as 1-2 μM). In some embodiments, the silicon-containing conjugate base to the silicon- containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final concentration of between 0.1 μM and 2.0 μM, between 0.5 μM and 2.0 μM, or between 1.0 μM and 2.0 μM. In some embodiments, the final concentration of the silicon-containing conjugate base to the silicon- containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final concentration of 1.5 μM. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 5 to (ii) number of thousand algal cells per ml multiplied by 50. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 15 to (ii) the number of thousand algal cells per ml multiplied by 35. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 20 to (ii) the number of thousand algal cells per ml multiplied by 30. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 22 to (ii) the number of thousand algal cells per ml multiplied by 26. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 5. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 10. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 15. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 20. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 25. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 30. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 40. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 50. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 5. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 10. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H4SiO4) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 15. In some embodiments, the silicon- containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 20. In some embodiments, the silicon-containing conjugate base to the silicon- containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 25. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 30. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 40. In some embodiments, the silicon-containing conjugate base to the silicon-containing acid (e.g. H ₄ SiO ₄ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 50. In some embodiments, silicon is added in the first algal culture phase to a final concentration of at least 0.15 μM, at least 0.5 μM, at least 1.0 μM, at least 1.5 μM, at least 2.0 μM, at least 5.0 μM, at least 10 μM, or at least 15 μM. In some embodiments, silicon is added in the first algal culture phase to a final concentration of 0.15-15 μM (e.g.0.5-4.5 μM, such as 1-2 μM). In some embodiments, silicon is added in the first algal culture phase to a final concentration of between 0.1 μM and 2.0 μM, between 0.5 μM and 2.0 μM, or between 1.0 μM and 2.0 μM. In some embodiments, silicon is added in the first algal culture phase to a final concentration of 1.5 μM. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 5 to (ii) number of thousand algal cells per ml multiplied by 50. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 15 to (ii) the number of thousand algal cells per ml multiplied by 35. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 20 to (ii) the number of thousand algal cells per ml multiplied by 30. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 22 to (ii) the number of thousand algal cells per ml multiplied by 26. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 5. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 10. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 15. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 20. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 25. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 30. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 40. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 50. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 5. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 10. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 15. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 20. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 25. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 30. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 40. In some embodiments, silicon is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 50. In some embodiments, a nitrogen-containing acid is added in the first algal culture phase. Nitrogen-fixing algae (e.g. diazotrophic phytoplankton or diatom-diazotroph assemblages) have a reduced requirement for assimilating nitrogen from the culture medium. Other algal species typically have a much greater need for nitrogen assimilation than for phosphorus assimilation from the culture medium. The average nitrogen to phosphorus ratio in algal biomass is 16:1. In some embodiments, the nutrient mineral acid is a nitrogen acid. In some embodiments, the nutrient mineral acid has a nitrate anion as a conjugate base. In some embodiments, the nutrient mineral acid is nitric acid, nitrous acid or hyponitrous acid. In preferred embodiments, the nitrogen-containing acid is nitric acid (HNO ₃ ). In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of at least 8 μM, at least 15 μM, at least 30 μM, at least 50 μM, at least 80 μM, at least 100 μM, at least 200 μM, at least 500 μM, or at least 800 μM. In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of 8-800 μM (e.g.20-320 μM, such as 60-100 μM). In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of between 50 μM and 100 μM, between 60 μM and 100 μM, between 70 μM and 100 μM, between 80 μM and 100 μM or between 80 μM and 90 μM. In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of 80 μM. The concentration of nitrogen-containing acid (e.g. HNO ₃ ) that is added can be influenced by the algal cell density. Accordingly, in some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 50 to (ii) number of thousand algal cells per ml multiplied by 5000. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 200 to (ii) the number of thousand algal cells per ml multiplied by 1500. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 400 to (ii) the number of thousand algal cells per ml multiplied by 800. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 600 to (ii) the number of thousand algal cells per ml multiplied by 700. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 50. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 100. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 200. In some embodiments, nitrogen- containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 400. In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 500. In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 600. In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 700. In some embodiments, nitrogen- containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 1000. In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 2000. In some embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 50. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 100. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 200. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 500. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 600. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 650. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 700. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 1000. In some embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 2000. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of at least 8 μM, at least 15 μM, at least 30 μM, at least 50 μM, at least 80 μM, at least 100 μM, at least 200 μM, at least 500 μM, or at least 800 μM. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of 8-800 μM (e.g.20-320 μM, such as 60-100 μM). In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of between 50 μM and 100 μM, between 60 μM and 100 μM, between 70 μM and 100 μM, between 80 μM and 100 μM or between 80 μM and 90 μM. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of 80 μM. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 50 to (ii) number of thousand algal cells per ml multiplied by 5000. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 200 to (ii) the number of thousand algal cells per ml multiplied by 1500. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 400 to (ii) the number of thousand algal cells per ml multiplied by 800. In some embodiments, the nitrogen- containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 600 to (ii) the number of thousand algal cells per ml multiplied by 700. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 50. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 100. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 200. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 400. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 500. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 600. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 700. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 1000. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 2000. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 50. In some embodiments, the nitrogen- containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 100. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 200. In some embodiments, the nitrogen- containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 500. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 600. In some embodiments, the nitrogen- containing conjugate base to the nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 650. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 700. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 1000. In some embodiments, the nitrogen-containing conjugate base to the nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 2000. In some embodiments, nitrogen is added in the first algal culture phase to a final concentration of at least 8 μM, at least 15 μM, at least 30 μM, at least 50 μM, at least 80 μM, at least 100 μM, at least 200 μM, at least 500 μM, or at least 800 μM. In some embodiments, nitrogen is added in the first algal culture phase to a final concentration of 8-800 μM (e.g.20-320 μM, such as 60-100 μM). In some embodiments, nitrogen is added in the first algal culture phase to a final concentration of between 50 μM and 100 μM, between 60 μM and 100 μM, between 70 μM and 100 μM, between 80 μM and 100 μM or between 80 μM and 90 μM. In some embodiments, nitrogen is added in the first algal culture phase to a final concentration of 80 μM. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 50 to (ii) number of thousand algal cells per ml multiplied by 5000. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 200 to (ii) the number of thousand algal cells per ml multiplied by 1500. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 400 to (ii) the number of thousand algal cells per ml multiplied by 800. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 600 to (ii) the number of thousand algal cells per ml multiplied by 700. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 50. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 100. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 200. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 400. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 500. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 600. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 700. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 1000. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as being at least the number of thousand algal cells per ml multiplied by 2000. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 50. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 100. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 200. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 500. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 600. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 650. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 700. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 1000. In some embodiments, nitrogen is added in the first algal culture phase to a final nanomolar concentration calculated as the number of thousand algal cells per ml multiplied by 2000. In some embodiments, one or more, two or more, three or more, four or more, or five or more nutrient mineral acids are added in the first algal culture phase. In some embodiments, the algae are diatoms, and a phosphorus-containing acid (e.g. H3PO4) a silicon-containing acid (H ₄ SiO ₄ ), and a nitrogen-containing acid (e.g. HNO ₃ ) are added in the first algal culture phase. In some embodiments, the algae are diatom-diazotroph assemblages, and a phosphorus-containing acid (e.g. H ₃ PO ₄ ) and a silicon-containing acid (H ₄ SiO ₄ ) are added in the first algal culture phase. In some embodiments, the algae are diazotrophic phytoplankton, and a phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase. In some embodiments, the algae are bloom-forming algae, and a phosphorus-containing acid (e.g. H ₃ PO ₄ ) and a nitrogen-containing acid (e.g. HNO ₃ ) are added in the first algal culture phase. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is at least 5 μM, at least 10 μM, at least 25 μM, at least 50 μM, at least 85 μM, at least 150 μM, at least 300 μM, at least 500 μM, or at least 850 μM. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is 5-850 μM (e.g.25-150 μM, such as 80-90 μM). In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is between 50 and 100 μM, between 60 and 100 μM, between 70 and 100 μM, between 80 and 100 μM or between 80 and 90 μM. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being within the range of: (i) number of thousand algal cells per ml multiplied by 50 to (ii) number of thousand algal cells per ml multiplied by 5000. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 200 to (ii) the number of thousand algal cells per ml multiplied by 1500. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 400 to (ii) the number of thousand algal cells per ml multiplied by 800. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being within the range of: (i) the number of thousand algal cells per ml multiplied by 600 to (ii) the number of thousand algal cells per ml multiplied by 700. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 50. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 100. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 200. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 400. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 500. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 600. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 700. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 1000. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as being at least the number of thousand algal cells per ml multiplied by 2000. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 50. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 100. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 200. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 500. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 600. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 650. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 700. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 1000. In some embodiments, the final concentration of total nutrient mineral acid(s) after addition of nutrient mineral acid(s) is calculated as the number of thousand algal cells per ml multiplied by 2000. In some embodiments, nutrient mineral acids are added in the first algal culture phase to achieve a pH value in the range of pH6.5-7.5. In the invention, no nutrient mineral acid is added in the second algal culture phase, such that the pH in the mariculture increases to at least pH 8.4. In some embodiments, the pH in the mariculture increases to at least pH 8.5, at least pH 8.6, at least pH 8.8, at least pH 9.0, at least pH 9.2, or at least pH 9.4. In some embodiments, the pH in the mariculture increases to pH 8.4-9.4 (e.g. pH 8.6-9.2). Algae In some embodiments, a single species of algae is cultured. In some embodiments, more than one species of algae is cultured. In some embodiments, the algae comprise diazotrophic phytoplankton. In some embodiments, the algae comprise assemblages of diazotrophic phytoplankton with other organisms. In some embodiments, the algae comprise diatom-diazotroph assemblages (DDAs). In some embodiments, the algae comprise diatoms. In some embodiments, the algae comprise bloom-forming algae. In some embodiments, the algae comprise r-strategist algae. Diazotrophic phytoplankton In some embodiments, the algae that are cultured in the method of the invention comprise diazotrophic phytoplankton. As used herein, “diazotrophic phytoplankton” refers to marine and freshwater nitrogen-fixing photosynthetic algae. Preferably, the diazotrophic phytoplankton are marine diazotrophic phytoplankton. In some embodiments, the diazotrophic phytoplankton belong to the Cyanobacteria phylum. Accordingly, in some embodiments the diazotrophic phytoplankton comprise cyanobacteria. In preferred embodiments, the diazotrophic phytoplankton is Trichodesmium sp. In some embodiments, the diazotrophic phytoplankton is one or more of T. erythraeum, T. contortum, T. hildebrandtii, T. radians, T. tenue, and T. thiebautii. In some embodiments, the diazotrophic phytoplankton is T. erythraeum. In some embodiments, the diazotrophic phytoplankton is Crocosphaera sp., optionally C. watsonii. In some embodiments, the diazotrophic phytoplankton is Calothrix sp., optionally C. adscendens, C. atricha, C. braunii, C. breviarticulata, C. caespitora, C. confervicola, C. crustacea, C. donnelli, C. elenkinii, C. epiphytica, C. fusca, C. juliana, C. parasitica, C. parietina, C. pilosa, C. pulvinata, C. scopulorum, C. scytonemicola, C. simulans, C. solitaria, C. stagnalis, C. stellaris, and C. thermalis. The inventors have found that culturing diazotrophic phytoplankton in land-based mariculture (e.g. in a raceway pond) under oligotrophic conditions results in especially efficient carbon sequestration. Oligotrophic conditions are nutrient poor conditions. For example, oligotrophic conditions may comprise low concentrations of bioavailable nitrogen and phosphorus. These oligotrophic conditions are preferably present within a raceway pond or a series of connected raceway ponds. In some embodiments, the oligotrophic conditions comprise a low concentration of nitrogen. In some embodiments, the oligotrophic conditions comprise a low concentration of nitrogen and phosphorus. In some embodiments, the oligotrophic conditions comprise a low concentration of bioavailable nitrogen. In some embodiments, the oligotrophic conditions comprise a low concentration of bioavailable nitrogen and phosphorus. Accordingly, in some embodiments the oligotrophic conditions comprise less than 20 µM, less than 10 µM or less than 5 µM phosphorus. Accordingly, in some embodiments the oligotrophic conditions comprise less than 40 µM, less than 20 µM, less than 15 µM, less than 10 µM or less than 5 µM nitrogen. In some embodiments, the oligotrophic conditions comprise less than 20 µM (e.g. 10 µM) phosphorus and less than 40 µM (e.g.20 µM) nitrogen. In some embodiments, the oligotrophic conditions comprise less than 10 µM (e.g.5 µM) phosphorus and less than 5 µM (e.g.1 µM) nitrogen. In some embodiments, DDAs (e.g. assemblages comprising Skeletonema sp.) are cultured and the oligotrophic conditions comprise less than 20 µM phosphorus and less than 30 µM silicate. In some embodiments, DDAs (e.g. assemblages comprising Skeletonema sp.) are cultured and the oligotrophic conditions comprise less than 10 µM phosphorus and less than 15 µM silicate. In some embodiments, DDAs comprising Hemiaulus sp. (e.g. assemblages of Richelia sp. and Hemiaulus sp.) are cultured and the oligotrophic conditions comprise less than 4 µM phosphorus, less than 2 µM nitrogen and less than 20 µM silicate. In some embodiments, DDAs comprising Hemiaulus sp. (e.g. assemblages of Richelia sp. and Hemiaulus sp.) are cultured and the oligotrophic conditions comprise less than 2 µM phosphorus, less than 1 µM nitrogen and less than 10 µM silicate. In some embodiments, diazotrophic phytoplankton (e.g. Trichodesmium sp.) are cultured and the oligotrophic conditions comprise less than 20 µM phosphorus and less than 40 µM nitrogen. In some embodiments, diazotrophic phytoplankton (e.g. Trichodesmium sp.) are cultured and the oligotrophic conditions comprise less than 10 µM phosphorus and less than 20 µM nitrogen. In some embodiments, diazotrophic phytoplankton (e.g. Trichodesmium sp.) are cultured and the oligotrophic conditions comprise less than 5 µM phosphorus and less than 10 µM nitrogen. In some embodiments, diazotrophic phytoplankton (e.g. Trichodesmium sp.) are cultured and the oligotrophic conditions comprise less than 1 µM phosphorus and less than 10 µM nitrogen. In some embodiments, the oligotrophic conditions are present on seeding diazotrophic phytoplankton and/or DDAs into the land-based mariculture and the oligotrophic conditions are maintained until harvesting of the diazotrophic phytoplankton and/or DDAs. In some instances, the oligotrophic conditions comprise less than 20 µM (e.g.10 µM) phosphorus and less than 40 µM (e.g.20 µM) nitrogen. Accordingly, in some embodiments of the invention, the algae comprise diazotrophic phytoplankton, and nutrient mineral acids are added to a total concentration of less than 60 µM (e.g. less than 30 µM). In some such embodiments, phosphorus- containing acid (e.g. H3PO4) is added in the first algal culture phase to a final concentration of less than 20 µM (e.g. less than 10 µM). In some such embodiments, nitrogen-containing acid (e.g. HNO3) is added in the first algal culture phase to a final concentration of less than 40 µM (e.g. less than 20 µM). In some embodiments, the oligotrophic conditions are present on seeding diazotrophic phytoplankton into the land-based mariculture and the oligotrophic conditions are maintained until harvesting of the diazotrophic phytoplankton. The culture of diazotrophic phytoplankton is discussed in more detail in International Patent Application No. PCT/GB2023/051392, incorporated herein by reference. DDAs In some embodiments, the algae that are cultured in the method of the invention comprise “diatom-diazotroph assemblages (DDAs)”. As used herein, “diatom-diazotroph assemblages (DDAs)” refers to symbioses between diatoms and diazotrophic prokaryotes. In these associations, the diazotrophic prokaryote captures or ‘fixes’ atmospheric N2 and makes it bioavailable to the diatom symbiont. In some embodiments, the DDAs comprise diazotrophic cyanobacteria. Diazotrophic cyanobacteria like Richelia, Calothrix and other unicellular species similar in morphology to free-living diazotroph Crocosphaera, thrive by forming symbiotic relationships with diatoms like Hemiaulus, Rhizosolenia, Chaetoceros and Climacodium (Mutalipassi et al., 2021; Hilton 2014). Some of these associations, like Calothrix or the novel unicellular cyanobacteria Candidatus Atelocyanobacterium thalassa (UCYN-A) (Tuo et al., 2017) associate with unicellular algae epiphytically (or on the outside of cells). Other diazotrophic symbionts are intracellular such as Richelia. In some embodiments, the DDAs comprise marine diazotrophic cyanobacteria. In some embodiments, the marine diazotrophic cyanobacteria are selected from Richelia sp., Calothrix sp., Crocosphaera sp. and Candidatus Atelocynaobacterium Thalassa. In some embodiments, the marine diazotrophic cyanobacteria are Richelia sp. In some embodiments, the marine diazotrophic cyanobacteria are Calothrix sp. In some embodiments, the marine diazotrophic cyanobacteria are Crocosphaera sp. In some embodiments, the marine diazotrophic cyanobacteria are Candidatus Atelocynaobacterium Thalassa. In some embodiments, the DDAs comprise Richelia sp., optionally R. intracellularis. In some embodiments, the DDAs comprise Calothrix sp., optionally one or more of C. adscendens, C. atricha, C. braunii, C. breviarticulata, C. caespitora, C. confervicola, C. crustacea, C. donnelli, C. elenkinii, C. epiphytica, C. fusca, C. juliana, C. parasitica, C. parietina, C. pilosa, C. pulvinata, C. scopulorum, C. scytonemicola, C. simulans, C. solitaria, C. stagnalis, C. stellaris, and C. thermalis. In some embodiments, the DDAs comprise Crocosphaera sp., optionally C. watsonii. In some embodiments, the DDAs comprise one or more of the following diatoms: Hemiaulus sp., Skeletonema sp., Rhizosolenia sp., Climacodium sp. and Chaetoceros sp. In some embodiments, the DDAs comprise Hemiaulus sp., optionally H. hauckii, H. indicus, H. membranaceus, or H. sinensis. In some embodiments, the DDAs comprise Skeletonema sp., optionally S. barbadense, S. costatum, S. cylindraceum, S. mediterraneum, S. punctatum, S. tropicum, or S. pseudocostatum. In some embodiments, the DDAs comprise Rhizosolenia sp., optionally R. alata, R. acuminata, R. antarctica, R. antennata, R. bergonii, R. clevei, R. curvata, R. cylindrus, R. delicatula, R. minima, R. pugens, R. robusta, R. rothii, R. stricta, or R. styliformis. In some embodiments, the DDAs comprise Climacodium sp., optionally C. biconcavum or C. frauenfeldianum. In some embodiments, the DDAs comprise Chaetoceros sp., optionally C. socialis, C. debilis, C. curvisetus, C. muelleri, C. calcitrans, or C. didymus. In some embodiments, the DDAs comprise an assemblage of marine diazotrophic cyanobacteria and diatoms. In some embodiments, the marine diazotrophic cyanobacteria are selected from Richelia sp., Calothrix sp., Crocosphaera sp. and Candidatus Atelocynaobacterium Thalassa, and the diatoms are selected from Hemiaulus sp., Skeletonema sp., Rhizosolenia sp., Climacodium sp. and Chaetoceros sp. In some embodiments, the DDAs comprise an assemblage of Richelia sp. and Hemiaulus sp. The inventors have found that culturing DDAs in land-based mariculture (e.g. in a raceway pond) under oligotrophic conditions results in especially efficient carbon sequestration. Oligotrophic conditions are nutrient poor conditions. For example, oligotrophic conditions may comprise low concentrations of bioavailable nitrogen and phosphorus. These oligotrophic conditions are preferably present within a raceway pond or a series of connected raceway ponds. In some embodiments, the oligotrophic conditions comprise a low concentration of nitrogen. In some embodiments, the oligotrophic conditions comprise a low concentration of nitrogen and phosphorus. In some embodiments, the oligotrophic conditions comprise a low concentration of bioavailable nitrogen. In some embodiments, the oligotrophic conditions comprise a low concentration of bioavailable nitrogen and phosphorus. Accordingly, in some embodiments the oligotrophic conditions comprise less than 20 µM, less than 10 µM or less than 5 µM phosphorus. Accordingly, in some embodiments the oligotrophic conditions comprise less than 40 µM, less than 20 µM, less than 15 µM, less than 10 µM or less than 5 µM nitrogen. In some embodiments, the oligotrophic conditions comprise less than 20 µM (e.g. 10 µM) phosphorus and less than 40 µM (e.g.20 µM) nitrogen. In some embodiments, the oligotrophic conditions comprise less than 10 µM (e.g.5 µM) phosphorus and less than 5 µM (e.g.1 µM) nitrogen. In some embodiments, DDAs (e.g. assemblages comprising Skeletonema sp.) are cultured and the oligotrophic conditions comprise less than 20 µM phosphorus and less than 30 µM silicate. In some embodiments, DDAs (e.g. assemblages comprising Skeletonema sp.) are cultured and the oligotrophic conditions comprise less than 10 µM phosphorus and less than 15 µM silicate. In some embodiments, DDAs comprising Hemiaulus sp. (e.g. assemblages of Richelia sp. and Hemiaulus sp.) are cultured and the oligotrophic conditions comprise less than 4 µM phosphorus, less than 2 µM nitrogen and less than 20 µM silicate. In some embodiments, DDAs comprising Hemiaulus sp. (e.g. assemblages of Richelia sp. and Hemiaulus sp.) are cultured and the oligotrophic conditions comprise less than 2 µM phosphorus, less than 1 µM nitrogen and less than 10 µM silicate. In some instances, the oligotrophic conditions comprise less than 20 µM (e.g.10 µM) phosphorus and less than 40 µM (e.g.20 µM) nitrogen. Accordingly, in some embodiments of the invention, the algae comprise DDAs, and nutrient mineral acids are added to a total concentration of less than 60 µM (e.g. less than 30 µM). In some such embodiments, phosphorus-containing acid (e.g. H ₃ PO ₄ ) is added in the first algal culture phase to a final concentration of less than 20 µM (e.g. less than 10 µM). In some such embodiments, nitrogen-containing acid (e.g. HNO ₃ ) is added in the first algal culture phase to a final concentration of less than 40 µM (e.g. less than 20 µM). In some embodiments, the oligotrophic conditions are present on seeding DDAs into the land-based mariculture and the oligotrophic conditions are maintained until harvesting of the DDAs. The culture of DDAs is discussed in more detail in International Patent Application No. PCT/GB2023/051392, incorporated herein by reference. Diatoms In some embodiments, the algae that are cultured in the method of the invention comprise diatoms. In some embodiments, the diatoms are fast-growing diatoms. In some embodiments, the diatoms are bloom-forming diatoms. For example, diatoms that have (i) the ability to grow exponentially or (ii) a cell division rate that exceeds one division per day. In some embodiments, the diatoms are selected from Skeletonema sp., Chaetoceros sp., Thalassiosira sp., Coscinodiscus sp., Navicula sp., Synedra sp. and Nitzschia sp. In some embodiments, the diatoms are Skeletonema sp., optionally S. barbadense, S. costatum, S. cylindraceum, S. mediterraneum, S. punctatum, S. tropicum, or S. pseudocostatum. In some embodiments, the diatoms are Chaetoceros sp., optionally C. socialis, C. debilis, C. curvisetus, C. muelleri, C. calcitrans, or C. didymus. In some embodiments, the diatoms are Thalassiosira sp., optionally T. pseudonana, or T. symmetrica. In some embodiments, the diatoms are Coscinodiscus sp., optionally C. wailesii. In some embodiments, the diatoms are Navicula sp., optionally N. pelliculosa, N. incerta, N. oblonga, N. salinicola, N. ramosissima, N. minima, N. cryptocephala, or N. trivialis. In some embodiments, the diatoms are Synedra sp., optionally S. capitata, S. famelica, S. radians, S. rumpens, or S. ulna. In some embodiments, the diatoms are Nitzschia sp., optionally N. frigida, N. acicularis, N. amphibia, or N. angustata. Bloom-forming algae In some embodiments, the algae that are cultured in the method of the invention comprise bloom-forming algae. In some embodiments, the bloom-forming algae are Dunaliella sp., optionally D. salina. In some embodiments, the bloom-forming algae are Chlorella sp., optionally C. vulgaris. In some embodiments, the bloom-forming algae are Spirulina sp. In some embodiments, the bloom-forming algae are Cryptomonas sp., optionally C. ovate. In some embodiments, the bloom-forming algae are Nannochlorpsis sp., optionally N. gaditana or N. oculate. In some embodiments, the bloom-forming algae are Tetraselmis sp. In some embodiments, the bloom-forming algae are Isochyrsis sp., optionally I. galbana. In some embodiments, the bloom-forming algae are Rhodomonas sp., optionally R. minuta. In some embodiments, the bloom-forming algae are Pyramimonas sp. In some embodiments, the bloom-forming algae are Microcystis sp., optionally M. aeruginosa. In some embodiments, the bloom-forming algae are Gymnodinium sp., optionally G. nagasakiense. In some embodiments, the bloom-forming algae are Chaetoceros sp., optionally C. socialis, C. debilis, C. curvisetus, C. muelleri, C. calcitrans, C. didymus, or C. convolutus. In some embodiments, the bloom-forming algae are Gonyaulax sp., optionally G. polygramma. R-strategist algae In ecology, r-strategist organisms are characterised by their high growth rates in less-crowded ecological niches. They are considered opportunistic organisms and thrive in more unstable and unpredictable environments due to their ability to reproduce rapidly. Conversely, K-strategist organisms are characterised by a much lower growth rate in an ecological niche which is close to or at the carrying capacity for that organism. They exist in an equilibrium and thrive in more stable or predictable environments, competing for limited resources. The method of the invention described herein represents a controlled, stable and predictable environment in which algae are cultured. Algae often fit the description of r-strategist organisms, displaying rapid growth rates in often unstable and unpredictable environments. Therefore, it is surprising to find that algae grow particularly well in the tightly controlled, highly predictable conditions of the method of the invention described herein. In some embodiments, the algae that are cultured in the method of the invention comprise r-strategist algae. In some embodiments, the r-strategist algae are cultured in a K-strategist environment. In some embodiments, the r-strategist algae are cultured under K-strategist conditions. In some embodiments, K-strategist conditions comprise one or more of a stable temperature, a stable salinity level, a stable humidity and a stable duration of sunlight. Raceway ponds Preferably, the land-based mariculture of the invention comprises culturing the algae in one or more raceway ponds. Preferably the one or more raceway ponds comprise seawater. A typical raceway pond is illustrated in Figure 3. Raceway pond is oblong shaped, with a partial divide in the middle of the pond (along the longitudinal axis) to create a circuit with at least two channels. At one end of this divide there is a support structure that serves both as an anchor for the paddlewheel, the platform for the CO ₂ equipment and to anchor the divider between the raceway channels. At the other end of the divide is a second flow diverter to ensure efficient flow throughout the raceway. Paddle wheel maintains the flow of water and algae around the circuit. In one embodiment, a covered raceway pond is a raceway pond covered by a greenhouse. The primary purpose of the greenhouse is to protect the seed algae from being contaminated by windborne or bird-borne contaminants. Secondly the greenhouse is used to raise the temperature of the algal growth environment; firstly to increase the algal growth rate, and secondly to inactivate competing or deleterious organisms that might otherwise contaminate the algae or foul the equipment. The greenhouse can also be used to selectively shade or change the illumination colour of the algae to induce a desirable physiological state by altering the light wavelength ratios. In one specific embodiment, every covered raceway pond is covered by a greenhouse. An open raceway pond has no external cover, and as such is fully exposed to the ambient atmosphere, while a covered raceway pond (which may be fully or partially covered) allows partial or complete control of the temperature and light environment. In one embodiment, each covered and/or open raceway pond has two channels. As raceway ponds increase in volume they have increased width and/or length and/or number of channels. In a specific embodiment, as open raceway ponds increase in volume they have increased width and length. In a specific embodiment, both covered and open raceway ponds have a width to length aspect ratio of between 1:4 and 1:12, preferably 1:8. At this ratio, there is relatively low head loss at each paddlewheel pumping station as the water circulates around the bends, favourable economy of the construction materials (straight walls are easier to build than the bends), the reduction of wind influence (wind fetch) as it blows across the pond (to prevent potentially unmixed zones). The width of approximately 30 metres per channel also reduces meandering flow to maintain turbulent flow. Information regarding the application of computational fluid dynamics to raceway pond design can be found in Kusmayadi, 2020. Paddlewheels may be used to maintain the flow of the algae and water around the covered and open raceway ponds. This is energy efficient whilst ensuring thorough mixing and the exposure of the algae to relatively low shear. This enables effective exchange of gases within the ambient air with the algae growth medium. According to the species being cultivated, different rate paddle wheels may be used. The paddlewheel rate may be 5-40 cm/sec, e.g.10-30 cm/sec, or 15-25 cm/sec. In one embodiment, each covered or open raceway pond preferably has 1 or 2, paddlewheels depending on the degree of agitation that is required. Preferably, each raceway pond has one paddlewheel. The paddlewheel may be positioned at any section of the raceway pond, but is preferably positioned closer to the narrower end of a raceway pond. Advantageously, paddlewheels agitate the ponds such that more carbon dioxide is absorbed across the air-pond surface interface. In one embodiment, one or more paddlewheel maintains the flow of the algae and water within a covered and/or open raceway pond at a rate of about 5-40 cm/sec, for example 10-30 cm/sec, or 15-25 cm/sec or 20 cm/sec, 25 cm/sec or 30 cm/sec. In one embodiment, a covered raceway pond has volume of between 50 l and 15,000,000 l, for example between 50 l and 50,000 l. In a particular embodiment, the volume of the covered raceway ponds in the series increases such that there is at least one pond in the series with a volume of (a) 50-1,000 l; at least one covered raceway pond in the series with a volume of (b) 1001-30,000 l; and at least one pond in the series with a volume of (c) 5,000 - 12,000,000 l. In one embodiment, these ponds are linked in a linear fashion, such that there is one pond at each stage in the series. In one embodiment, an open raceway pond has volume of between 1,500,000 l and 3,000,000 l, in a further embodiment between 6,000,000 l and 15,000,000 l. In a still further embodiment, the volume of the open raceway ponds in the series increases such that there is at least one open raceway pond in the series with a volume of (a) 360,000 – 720,000 l; at least one pond in the series with a volume of (b) 1,500,000 - 3,000,000 l; and at least one pond in the series with a volume of (c) 6,000,000 – 15,000,000 l. The depth of a raceway pond affects algal solar irradiation. Both light intensity and the light wavelength ratio are altered by increasing water depth. In general, far red, red and ultraviolet light are absorbed the most rapidly by the water and a blue and green light penetrate the furthest. In one embodiment, a covered or open raceway pond is between 0.05 m and 10 m deep, for example, 0.05 m, 0.10 m, 0.20 m, 0.30 m, 0.40 m, 0.50m, 0.60 m, 0.70 m, 0.80 m, 0.90 m, 1m, 1.5m, 2 m, 3 m, 5 m, or 10 m deep. In one embodiment, a covered raceway pond is 0.1m – 1m deep, for example 0.1m, 0.2m, 0.3m, 0.4m, or 0.5m deep. In one embodiment, an open raceway pond is 0.25 or 0.3 m – 1 m deep, for example 0.25 m, 0.3 – 0.4m, 0.5 m, 0.75 or 1 m deep. Preferably an open raceway pond is less than 1 m deep. At this depth there is sufficient outgassing of O ₂ to help reduce oxidative stress, also at this depth there is sufficient exposure to dissolve atmospheric CO ₂ . Raceway ponds known in the art are also usually uniform in depth. However, the present inventor has discovered that if the depth of a raceway pond is varied along the length of a channel or between adjacent channels, a change in the flow rate results. Furthermore, the exposure of the algae to solar irradiation is varied, with algae in shallower areas of the raceway pond experiencing greater light intensity and a greater proportion of red light than algae in deeper areas. Photosynthetic output can be affected by the light ratio, especially at dawn and dusk, and as discussed herein the depth of the water alters the light wavelength ratio. Thus, in one embodiment, the depth of an open raceway pond is non-uniform, resulting in a change in algal exposure to light both in terms of light intensity and light wavelength ratio and/or a change in the rate of gas exchange within the non-uniform section of the raceway pond. In one embodiment, the difference between the depth in adjacent channels is 0.05-1.0 m, for example 0.05 m, 0.10 m, 0.2 m, 0.3 m, 0.4 m, 0.5 m, 0.6 m, 0.7 m, 0.8 m, 0.9 m or 1.0 m. For example, one channel is 0.2- 0.5 m deep, while the adjacent channel is 0.8-1.0 m deep. As described herein, the raceway ponds of the present invention may be lined. In one embodiment, covered and open raceway ponds are lined with an impermeable material. If seawater is used to culture the algae, a clay lining may be used to prevent saltwater intrusion onto the land. In one embodiment, a plastic waterproof lining is used instead of, or in addition to, a clay lining. In a particular embodiment, each raceway pond is lined with 10-20 cm of clay and a 2-5 cm, e.g. about 3 cm or specifically 8, 10 or 12 mm, robust synthetic liner such as white HDPE geomembrane. In one embodiment, the colour of the pond liners may also be chosen to alter the light wavelength ratio experienced by the algae as it reflects off the bottom of the ponds. The colour of the liner may selectively increase or decrease exposure of the algae to underwater red (630-680 nm), far red (700- 750 nm) and/or blue (400-450 nm) light. In one embodiment, the liner selectively increases the exposure to underwater red (630-680 nm), far red (700-750 nm) and/or blue (400-450 nm) light by 10-90%, 20-80%, 30-70%, or 40-60%. For example, the liner may selectively absorb up to 10, 20, 30, 40, 50, 60, 70, 80, 90 or 100% of the incident underwater red (630-680 nm), far red (700-750 nm) and/or blue (400-450 nm) light before the remaining light is reflected through the algal growth environment again. In a second embodiment, the lining is white in order to reflect light off the bottom and maximise the light available for photosynthesis and encourage algal growth especially in the low density cultures and/or shallow cultures less than 30cm deep, where light will penetrate the depth of the medium. In some instances, black liners may be used to deliberately increase the temperature of the cultivation medium. Different colours of lining may be used to induce different physiological effects in the algae. For example, the lining may be entirely red, blue or green. Alternatively, a single stage in the sequence of ponds can be coloured blue, for example at the point where the seed algal growth has been synchronised in the initial covered ponds, to reinforce cellular growth synchronisation and increase growth before cell division, just before the cells are introduced into the open growth ponds so that multiple divisions then occur in the growth pond. Similarly, the growth pond can be lined in blue to stimulate the migration of chloroplasts to the outside of the cells, to promote maximum photosynthesis (Kraml & Hermann, 1991; Furukawa et al., 1998). Another typical raceway pond is illustrated in Figure 1. Raceway pond 100 is stadium shaped (i.e., a rectangle with semicircles at a pair of opposite ends), with a partial divide in the centre of the pond 100 (i.e., along the longitudinal axis A) to create a circuit (i.e., channel 120) having two longitudinal channel sections 120a, 120b which are joined at opposite ends of the raceway pond 100 by U shaped channel sections 120c, 120d. The stadium shape is defined by side wall 102. The partial divide is defined by divider 104. The side wall 102 and divider 104 may be formed of plastic covered and reinforced walls, fencing posts or earthen berms. Water and algae are retained in the raceway pond 100 by the side wall 102 and the base of the pond (not shown). At one side of divider 104 (e.g., along a side wall 102) there may be a support structure that serves both as an anchor for a paddlewheel 110, a platform for CO2 sequestering equipment (not shown) and to anchor the divider 104 between the longitudinal channel sections 120a, 120b. Paddlewheel 110 maintains the flow of water and algae around the circuit. The paddlewheel 110 is typically a variable speed paddlewheel. At the opposite ends of the raceway pond 100 (i.e., at the semicircles of the stadium shape), the channel has U-shaped channel sections 120c, 120d. Within the U-shaped channel sections 120c, 120d, there are flow diverters 106 to ensure efficient flow throughout the raceway. Flow diverters 106 act to maintain laminar flow of algae and water around the channel 120, especially at the U shaped channel sections 120c, 120d. The raceway pond 100 further comprises an inlet pipe 108 and a drainpipe 112. The inlet pipe 108 may be connected to a gate-controlled sluice (not shown) for pond intake from either a seawater canal and/or a previous pond. The drainpipe 112 facilitates pond discharge through a second gate- controlled sluice (not shown). The dilution rate of the algae in the raceway pond 100, which is the rate at which water is added to the algae (i.e., to dilute the algae), is determined by the position of the gate-controlled sluice of the inlet pipe 108 and/or the drainpipe 112. For instance, opening the gate-controlled sluice of the inlet pipe 108 and closing the gate-controlled sluice of the drainpipe 112 increases the dilution rate. The dilution volume is the volume of water added to the already partially filled raceway pond. In one embodiment, raceway pond 100 may be a covered raceway pond, which is a raceway pond 100 covered by a greenhouse (not shown). The primary purpose of the greenhouse is to protect the seed algae from being contaminated by windborne or bird-borne contaminants. Secondly the greenhouse is used to raise the temperature of the algal growth environment; both to increase the algal growth rate, and to inactivate competing or deleterious organisms that might otherwise contaminate the algae or foul the equipment. The greenhouse can also be used to selectively shade or change the illumination colour of the algae to induce a desirable physiological state by altering the wavelength of light. In one specific embodiment, every raceway pond 100 is covered by a greenhouse. Alternatively, raceway pond 100 may be an open raceway pond. An open raceway pond has no external cover, and as such is fully exposed to the ambient atmosphere, while a covered raceway pond (which may be fully or partially covered) allows partial or complete control of the temperature and light environment. Each raceway pond 100 is able to hold a certain volume of water and algae, depending on the depth, width and length of the raceway pond 100. In the context of the invention, volume of a raceway pond is defined as its capacity (i.e., the volume of fluid a raceway pond is capable of holding) rather than the volume of fluid actually held in the raceway pond at any given time. An increase in volume of raceway pond 100 is achieved by increased width and/or length of the raceway pond. In a specific embodiment, raceway pond 100 increases in volume through increased width and length. Depth of the raceway pond 100 cannot be increased as easily since changing the depth affects algal solar irradiation. In a specific embodiment, raceway pond 100 has a width (perpendicular to axis A) to length (along axis A) size ratio of between 1:4 and 1:12, preferably 1:8. At this ratio, there is relatively low head loss at each paddlewheel 110 as the water circulates around the bends, favourable economy of the construction materials (straight walls are easier to build than the bends), the reduction of wind influence (wind fetch) as it blows across the pond (to prevent potentially unmixed zones). The width of approximately 30 metres per channel 120 also reduces meandering flow to maintain turbulent flow. Information regarding the application of computational fluid dynamics to raceway pond design can be found in Kusmayadi, 2020. In some embodiments, a plurality of raceway ponds 100 may be used in parallel to increase the collective volume of water and algae. The plurality of raceway ponds 100 may form a group. The group may comprise, for example, 2, 4, 6, 8, 10, 12, 14, 16, or 18 ponds. The inlet pipe 108 of each raceway pond 100 of the group may connected to a common seawater canal. Similarly, the drainpipe 112 of each raceway pond 100 of the group may connected to a common outlet. In one embodiment, a covered raceway pond (or group of covered raceway ponds) has volume of between 50 l and 15,000,000 l, for example between 50 l and 50,000 l. In a particular embodiment, there is a series of covered raceway ponds, and the volume of covered raceway ponds in the series increases such that there is at least one pond in the series with a volume of (a) 50-1,000 l; at least one covered raceway pond in the series with a volume of (b) 1001-30,000 l; and at least one pond in the series with a volume of (c) 5,000 - 12,000,000 l. In one embodiment, these ponds are linked in a linear fashion, such that there is one pond at each stage in the series. In one embodiment, an open raceway pond (or group of open raceway ponds) has volume of between 1,500,000 l and 3,000,000 l, in a further embodiment between 6,000,000 l and 15,000,000 l. In a still further embodiment, the volume of the open raceway ponds in the series increases such that there is at least one open raceway pond in the series with a volume of (a) 360,000 – 720,000 l; at least one pond in the series with a volume of (b) 1,500,000 - 3,000,000 l; and at least one pond in the series with a volume of (c) 6,000,000 – 15,000,000 l. As mentioned, paddlewheel 110 may be used to maintain the flow of the algae and water around the raceway pond 100. This is energy efficient whilst ensuring thorough mixing and the exposure of the algae to relatively low shear. This enables effective exchange of gases within the ambient air with the algae growth medium. According to the species being cultivated, paddlewheel 100 may be used to achieve a different flow rate of algae and water within a raceway pond based on the physical attributes of the paddlewheel (e.g., number of paddles, size of paddles) and/or the paddlewheel speed (i.e., its rotational speed). The flow rate may be 0.1-0.5 m/minute, e.g., 0.1-0.4 m/minute or 0.1-0.3 m/minute. In one embodiment, each raceway pond 100 has one or more paddlewheels 110 depending on the degree of agitation that is required. Preferably, each raceway pond 100 has one paddlewheel 110. The paddlewheel 110 may be positioned at any section of the raceway pond, but is preferably positioned close to the inlet pipe 108 of a raceway pond (e.g., where the rectangle section of the stadium shape transitions to a semicircle). In one embodiment, one or more paddlewheels 110 maintain the flow of the algae and water within raceway pond 100 at a rate of about 0.1-0.5 m/minute, for example 0.1-0.4 m/minute, or 0.1-0.3 m/minute, or 0.15 m/minute, 0.2 m/minute, 0.25 m/minute. The depth of raceway pond 100 affects algal solar irradiation. Both light intensity and wavelengths are altered by increasing water depth. In general, far red, red and ultraviolet light are absorbed the most rapidly by the water and a blue and green light penetrate the furthest. However, algae in a shallower raceway pond 100 experiences greater light intensity and a greater proportion of red light than algae in a deeper raceway pond 100. In one embodiment, raceway pond 100 is between 0.05 m and 10 m deep, for example, 0.05 m, 0.10 m, 0.20 m, 0.30 m, 0.40 m, 0.50 m, 0.60 m, 0.70 m, 0.80 m, 0.90 m, 1 m, 1.5 m, 2 m, 3 m, or 5 m deep. In one embodiment, a covered raceway pond is 0.1–1 m deep, for example 0.1 m, 0.2 m, 0.3 m, 0.4 m, or 0.5 m deep. In one embodiment, an open raceway pond is 0.25 m or 0.3–1 m deep, for example 0.25 m, 0.3–0.4 m, 0.5 m, 0.75 m or 1 m deep. Preferably an open raceway pond is less than 1 m deep. At this depth there is sufficient outgassing of O2 to help reduce oxidative stress, also at this depth there is sufficient exposure to dissolve atmospheric CO2. Raceway ponds known in the art are also usually uniform in depth. However, if the depth of raceway pond 100 is varied along the length of channel 120 (e.g., between longitudinal channel sections 120a, 120b), a change in the flow rate results. Furthermore, the exposure of the algae to solar irradiation is varied, with algae in shallower areas of the raceway pond experiencing greater light intensity and a greater proportion of red light than algae in deeper areas. Photosynthetic output can be affected by the light ratio, especially at dawn and dusk, and as discussed herein the depth of the water alters the light wavelength ratio. Thus, in one embodiment, the depth of raceway pond 100 is non-uniform, resulting in a change in algal exposure to light both in terms of light intensity and light wavelength ratio and/or a change in the rate of gas exchange within the non-uniform section of the raceway pond. In one embodiment, the difference between the depth in longitudinal channel sections 120a, 120b is 0.05-1.0 m, for example 0.05 m, 0.10 m, 0.2 m, 0.3 m, 0.4 m, 0.5 m, 0.6 m, 0.7 m, 0.8 m, 0.9 m or 1.0 m. For example, one longitudinal channel section 120a is 0.2-0.5 m deep, while the second longitudinal channel section 120b is 0.8-1.0 m deep. As described herein, raceway pond 100 may be lined (not shown). In one embodiment, raceway pond 100 is lined with an impermeable material. If seawater is used to culture the algae, a clay lining may be used to prevent saltwater intrusion onto the land. In one embodiment, a plastic waterproof lining is used instead of, or in addition to, a clay lining. In a particular embodiment, each raceway pond 100 is lined with 10-20 cm of clay and a 2-5 cm, e.g., about 3 cm or specifically 8, 10 or 12 mm, robust synthetic liner such as a black or white geomembrane. A white coating, for instance from titanium oxide, may be provided over the black geomembrane. In one embodiment, the colour of the pond liners, or a coating of the pond liners, may be chosen to alter the wavelengths of light received by the algae as light reflects off the base of the ponds. The colour of the liner or coating may selectively decrease exposure of the algae to underwater red (630- 680 nm), far red (700-750 nm) and/or blue (400-450 nm) light. In one embodiment, the liner or coating selectively decreases the exposure to underwater red (630-680 nm), far red (700-750 nm) and/or blue (400-450 nm) light by 10-90%, 20-80%, 30-70%, or 40-60%. For example, the liner or coating may selectively absorb up to 10, 20, 30, 40, 50, 60, 70, 80, 90 or 100% of the incident underwater red (630-680 nm), far red (700-750 nm) and/or blue (400-450 nm) light before the remaining light is reflected through the algal growth environment again. This is achieved by selecting the colour of the pond liner or coating based on the wavelengths that are to be absorbed. In a second embodiment, the lining or coating is white in order to reflect light off the base of the pond and maximise the light available for photosynthesis and encourage algal growth especially in the low-density cultures and/or shallow cultures less than 30cm deep, where light will penetrate the depth of the medium. In some instances, black liners may be used to deliberately increase the temperature of the cultivation medium. Different colours of lining or coating may be used to induce different physiological effects in the algae. For example, the lining or coating may be entirely red, blue or green. Alternatively, a single stage in the sequence of ponds can be coloured blue, for example at the point where the seed algal growth has been synchronised in the initial covered ponds, to reinforce cellular growth synchronisation and increase growth before cell division, just before the cells are introduced into the open growth ponds so that multiple divisions then occur in the growth pond. Similarly, the growth pond can be lined or coated in blue to stimulate the migration of chloroplasts to the outside of the cells, to promote maximum photosynthesis (Kraml & Hermann, 1991; Furukawa et al., 1998). As an alternative to coloured lining or coating, the side wall 102, base and other structural features within the pond may be coloured. For instance, the side wall 102, base and other structural features may be white. Series of raceway ponds In one embodiment, the land-based mariculture of the invention comprises culturing algae in a series of connected raceway ponds, arranged in stages. The raceway ponds are connected in such a way so as to allow water and algae to pass directly between raceway ponds in successive stages of the series. However, the connection between raceway ponds can be closed and each raceway pond can be an isolated growth environment. The flow of water and algae between successive stages in the series is unidirectional, i.e. the passage of algae and water through the connected series of raceway ponds is one-way and algae and water are not re-circulated. In one specific embodiment of the invention the series of connected raceway ponds comprises firstly, one or more stages of covered raceway ponds and secondly, one or more stages of open raceway ponds. The designations of “firstly” one or more stages of covered raceway ponds and “secondly” one or more stages of open raceway ponds indicate that within the series of connected ponds, the stages comprising covered raceway ponds will always come before the stages comprising open raceway ponds. Put another way, an open raceway pond will never be succeeded by a covered raceway pond. The present inventor has found that successive dilution in a semi-continuous cultivation manner, which maintains a low algal cell density, is beneficial for maintaining algae in the exponential growth phase. Successive dilution can be achieved in two ways. In the first way dilution is achieved by increasing the collective volume of the raceway ponds in each stage of the series. This increase in collective volume can be achieved by increasing the volume of the individual raceway ponds in each successive stage of the series and/or by increasing the number of raceway ponds in each successive stage of the series. Thus, at each successive stage in the series of raceway ponds of the present invention, each individual raceway pond has a volume greater than the volume of the individual raceway ponds in the preceding stage of the series; and/or each raceway pond is immediately succeeded by a greater number of raceway ponds, wherein the collective volume of the raceway ponds in any given stage exceeds the collective volume of the raceway ponds of the preceding stage. In the second way, dilution is achieved by increasing the volume in stages to a maximum volume within a pond, before the water and algae are transferred to the subsequent larger pond. In the embodiment outlined in the model and table below, each pond is initially filled to a depth of 0.25 m where the cells complete a growth cycle. When it is time to double the volume of the water, to enable the cells to grow at a low standing stock with natural nutrients, the depth of the same pond is increased to 0.5 m. After the second growth cycle is complete within that pond, the total volume of the two division stages and the seawater is transferred to the next larger, subsequent pond. In other embodiments, the pond is filled in subsequent stages to 0.25 m, 0.5 m, 0.75 m and 1 m depth in four sequential ‘within-pond’ dilutions before it is transferred to the next larger pond. This ‘stacking’ of ponds is possible because of the relatively low standing stock (or low cellular concentration) of the algae in comparison to other cultivation systems. In other commercial algal growth systems (where cells are grown at a density resulting between 1,000 – 2,000 mg Chl a m ^-3 ), the high cell density results in gas exchange limitations and self-shading. However in this method, neither of these are critical concerns, because the cell densities are significantly lower for the first 12-16 growth cycles resulting in 50, 100, 200, 300, 400, 500 mg Chl a m ^-3 ). At these Chl a concentrations, the ponds can be run without cell shading and the natural capacity of the seawater to absorb and buffer gases as well as exchange gases with the atmosphere enables cell growth. In the context of this invention, the volume of a raceway pond is defined as its capacity (i.e. the volume of fluid a raceway pond is capable of holding) rather than the volume of fluid actually held in the raceway pond at any given time. When algae and water are transferred from a raceway pond (covered or open) in one stage of the series to one or more raceway ponds (covered or open) in the next stage of the series, either the algae and water are transferred to a single raceway pond with a greater volume, or the algae and water are divided between a number of raceway ponds with a larger collective volume. Each transfer of the algae and water from one stage of the series to the next stage in the series thus involves dilution of the algae or is preceded by dilution of the algae in the current stage of ponds. In one embodiment, when the algae and water from one stage in the series is used to seed the raceway pond or raceway ponds of the next stage, it is transferred to the raceway pond or raceway ponds of larger volume in the next stage of the series. Water is added to, or is already present in, the raceway ponds to be seeded, such that the final volume of fluid within the raceway ponds after seeding is equal to its capacity. This seeding step results in the algae being diluted and a low algal cell density can thus be maintained. Maintaining this constant low cell density of algae prevents the problems associated with traditional high-density algal culture, such as quorum sensing, biofilm formation and other (often unpredictable) algal stress responses. In an alternative embodiment, the algae are diluted prior to being transferred to the next stage of ponds. In this embodiment, fresh seawater is added to the current stage of ponds to dilute the algae. The successive dilution of the algae at each seeding step should not be taken to mean that the algal cell density at each stage in the series is successively reduced. Since the algae multiply rapidly, despite the successive dilutions at each seeding step the approximate cell density of algae in each stage of raceway ponds going through the series may increase, decrease or remain the same. In a specific embodiment, there are at least two stages of covered raceway ponds in the series of connected raceway ponds. For example, there may be 2, 3, 4, 5, 6, 7, 8, 9, 10, 15 or 20 stages of covered raceway ponds. In one embodiment, there are 2-10 stages of covered raceway ponds, 4-8 stages of covered raceway ponds, or 5 stages of covered raceway ponds. In a preferred embodiment, the covered raceway ponds are preferably greenhouse covered and are connected in linear succession, wherein there is one covered raceway pond at each stage in the series of covered raceway ponds. In this embodiment, each covered raceway pond is at least 2 times, for example 2 to 5 times, the volume of the covered raceway pond of the previous stage in the series. In a specific embodiment, each covered raceway pond is 2, 3, 4, or 5 times volume of the covered raceway pond of the previous stage in the series. In a preferred embodiment, each covered raceway pond is 5 times volume of the covered raceway pond of the previous stage in the series. In a further specific embodiment, there are at least two stages of open raceway ponds in the series of connected raceway ponds. For example, there may be 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20 or 25 stages of open raceway ponds. In one embodiment, there are 2-10 stages of open raceway ponds, 4-6 stages of open raceway ponds, or 5 stages of open raceway ponds. In one specific embodiment, there are more open raceway ponds than closed raceway ponds in the series. In a particular embodiment, the number of open raceway ponds in each stage increases at each successive stage in the series. In this embodiment, each open raceway pond is connected to two or more open raceway ponds in the next stage in the series, and the collective volume of each of the two or more open raceway pond exceeds the volume of the raceway pond in the preceding stage. Therefore, in this particular embodiment, the algae and water in one open raceway pond is diluted into two or more open raceway ponds when the algae and water are transferred between stages in the series. In a specific embodiment, the number of open raceway ponds in each stage of the series doubles. Therefore, in this embodiment the number of raceway ponds at each stage in the series increases exponentially. For example, the number of open raceway ponds at each stage increases as follows: 1, 2, 4, 8, 16, 32, 64, 128. In this embodiment, as the number of open raceway ponds at each stage increases, so does the volume of each individual raceway pond. In a preferred embodiment, the volume of the individual open raceway ponds in one stage is at least two times, preferably five times, the volume of the individual open raceway ponds in the previous stage. In an alternative embodiment, the volume of the individual open raceway ponds at each stage in the series remains the same, although the collective volume of the raceway ponds increases with each stage as the number of raceway ponds increases. The algae and water may be transferred between raceway ponds in successive stages of the series without any external force, for example it may be transferred under the influence of gravity. However, the algae and water will, on occasion when the local topography does not permit the use of gravity transfers, be pumped from one raceway pond to another, using any suitable pumping means that does not shear the cells. Figure 4 illustrates the layout of a specific algal cultivation system, including the seawater pipe that is used to fill an elevated seawater canal. This seawater canal feeds a series of raceway ponds. Each pond has a connection to at least the elevated seawater canal and a lower lying subsequent pond through a gate controlled sluice pond discharge. The series of ponds commences with small covered seed ponds to grow the inoculums. Each subsequent pond has at least twice the capacity of the previous pond to hold the entirety of the volume of the previous pond and the equivalent volume of unused seawater. The layout in figure 2 has two stages with four channels including the “return channel”). One set of raceway pond with eight channels, including the “return channel, and one set with 10 channels including the “return channels”. This final set drains into two large and deep harvesting ponds . The advantage of this oblong layout is that it efficiently hugs the coast along the edge of an ocean and enables each pond to have at least one contact with the elevated seawater canal and a discharge into the next larger and lower pond. This layout enables the water transfer within the entire pond system to rely on gravity feeds and requires a minimum of piping, while enabling easier maintenance of the ponds. This layout also takes advantage of the frequently encountered natural gradient along coastlines where distance from the shore commonly results in a slight increase in elevation. Finally, the intake manifold is upstream and as far as possible from the discharge system to avoid reuptake of already spent seawater. In another embodiment, the land-based mariculture of the invention comprises culturing the algae in a series of connected raceway ponds, arranged in stages, optionally wherein each of the raceway ponds in the series of connected raceway ponds may be based on raceway pond 100 of Figure 1. An example of an algal cultivation system 200 comprising a series of connected raceway ponds 210 arranged in stages 210A-230E is illustrated in Figure 2A. Figure 2B shows subsystem 200’ of system 200 in further detail. The stages 210A-230E of raceway ponds are connected in such a way so as to allow water and algae to pass directly between raceway ponds 100 in successive stages of the series. However, the connection between the stages 210A-230E of raceway ponds 100 can be closed and each stage 210A-230E of raceway ponds can be an isolated growth environment. The flow of water and algae between successive stages in the series is unidirectional, i.e., the passage of algae and water through the connected series of raceway ponds is one-way and algae and water are not re-circulated. In particular, in Figures 2A and 2B, there are three stages of covered raceway ponds, 210A, 210B and 210C and two stages of open raceway ponds 210D, 210E. However, other numbers of stages of covered raceway ponds and open raceway ponds may be used. In one specific embodiment of the invention the series of connected raceway ponds 210 comprises firstly, one or more stages of covered raceway ponds 210A-210C and secondly, one or more stages of open raceway ponds 210D-210E. The designations of “firstly” one or more stages of covered raceway ponds 210A-210C and “secondly” one or more stages of open raceway ponds 210D-210E indicate that within the series of connected ponds 210, the stages comprising covered raceway ponds 210A-210C will always come before the stages comprising open raceway ponds 210D-210E. Put another way, an open raceway 210A-210C pond will never be succeeded by a covered raceway pond 210D-210E. Each stage 210A-210E of the series of connected raceway ponds 210 may comprise one or more raceway ponds 100. Stages having a plurality (or group) of raceway ponds 100 use these ponds in parallel to increase the collective volume of water and algae that is throughput. The system 200 in Figures 2A and 2B, there are 16 ponds in each stage 210A-210E. However, the number of ponds does not have to be the same for each stage, as discussed further herein. In addition to the series of connected raceway ponds 210, system 200 comprises an intake pipeline 202 to transport water to the system, typically seawater from the ocean. Intake pipeline 202 feeds intake canal 208 which provides each of the raceway ponds in the series of connected raceway ponds 210 with water. Each raceway pond 100 has a connection to supply canal 208 at its respective inlet pipe 108. The supply canal 208 may be elevated so that gravity can be used to transport water to each of the raceway ponds 100 via the inlet pipe 108. The elevated supply canal filled from intake pipeline 202 with high-rate, low-head pumps. System 200 also comprises a harvest canal 212. Each raceway pond 100 in at least the final stage of the series of connected raceway ponds 210 has a connection to harvest canal 212 at its respective drainpipe 112. In stages other than the final stage, each raceway pond 100 is connected to the next stage of raceway ponds via its respective drainpipe 112. The harvest canal 212 leads to a harvesting building 214, where the algae are collected. The spent water is discharged through discharge pipeline 216. The discharge pipeline is at low elevation so that gravity moves water out of the harvesting building 214. In embodiments where the water is seawater, the intake pipeline 202 is upstream and as far needed from the discharge pipeline 216 to avoid reuptake of already spent seawater. Successive dilution in a semi-continuous cultivation manner, which maintains a low algal cell density, is beneficial for maintaining algae in the exponential growth phase. Two exemplary ways for achieving successive dilution are described below. In the first way, dilution is achieved by increasing the collective volume of the raceway pond(s) 100 in each stage 210A-210E of the series. This increase in collective volume can be achieved by increasing the volume of the individual raceway ponds in each successive stage 210A-210E of the series and/or by increasing the number of raceway ponds in each successive stage 210A-210E of the series. Thus, at each successive stage 210A-210E in the series of raceway ponds 210 of the present invention, each individual raceway pond has a volume greater than the volume of the individual raceway ponds in the preceding stage of the series; and/or each raceway pond is immediately succeeded by a greater number of raceway ponds, wherein the collective volume of the raceway ponds in any given stage exceeds the collective volume of the raceway ponds of the preceding stage. In the second way, dilution is achieved by increasing the volume of water in discrete steps to a maximum volume within a raceway pond 100, before the water and algae are transferred to the subsequent larger pond(s). For example, each pond may be initially filled to a first volume having a first depth (e.g., 0.25 m) where the cells complete a growth cycle. When it is time to increase (e.g., double) the volume of the water, to enable the cells to grow at a low standing stock with natural nutrients, the volume of water of the same pond is increased to a second volume having a second depth (e.g., 0.5 m). After the second growth cycle is complete within that pond, the total volume of the two division stages and the water is transferred to the next larger, subsequent pond. In other embodiments, the pond is filled in subsequent stages to 0.25 m, 0.5 m, 0.75 m and 1 m depth in four sequential ‘within-pond’ dilutions before it is transferred to the next larger pond. This ‘stacking’ of ponds is possible because of the relatively low standing stock (or low cellular concentration) of the algae in comparison to other cultivation systems. In other commercial algal growth systems (where cells are grown at a density resulting between 1,000 – 2,000 mg Chl a m-3), the high cell density results in gas exchange limitations and self-shading. However, in this method, neither of these are critical concerns, because the cell densities are significantly lower for the first 12-16 growth cycles resulting in 50, 100, 200, 300, 400, 500 mg Chl a m-3). At these Chl a concentrations the ponds can be run without cell shading and the natural capacity of the seawater to absorb and buffer gases as well as exchange gases with the atmosphere enables cell growth. When algae and water are transferred from a raceway pond (covered or open) in one stage of the series to one or more raceway ponds (covered or open) in the next stage of the series, either the algae and water are transferred to a single raceway pond with a greater volume, or the algae and water are divided between a number of raceway ponds with a larger collective volume. Each transfer of the algae and water from one stage of the series to the next stage in the series thus involves dilution of the algae or is preceded by dilution of the algae in the current stage of ponds. In one embodiment, when the algae and water from one stage in the series (e.g., stage 210A) is used to seed the raceway pond or raceway ponds of the next stage (e.g., stage 210B), it is transferred to the raceway pond or raceway ponds of larger volume in the next stage of the series. Water is added to, or is already present in, the raceway ponds to be seeded, such that the final volume of fluid within the raceway ponds after seeding is equal to its capacity. This seeding step results in the algae being diluted and a low algal cell density can thus be maintained. Maintaining this constant low cell density of algae prevents the problems associated with traditional high-density algal culture, such as quorum sensing, biofilm formation and other (often unpredictable) algal stress responses. In an alternative embodiment, the algae are diluted prior to being transferred to the next stage of ponds. In this embodiment, fresh seawater is added to the current stage of ponds to dilute the algae. The successive dilution of the algae at each seeding step should not be taken to mean that the algal cell density at each stage in the series is successively reduced. Since the algae multiply rapidly, despite the successive dilutions at each seeding step the approximate cell density of algae in each stage of raceway ponds 210A-210E going through the series may increase, decrease or remain the same. In a specific embodiment, there are at least two stages of covered raceway ponds in the series of connected raceway ponds. For example, there may be 2, 3, 4, 5, 6, 7, 8, 9, 10, 15 or 20 stages of covered raceway ponds. In one embodiment, there are 2-10 stages of covered raceway ponds, 4-8 stages of covered raceway ponds, or 5 stages of covered raceway ponds. In a preferred embodiment, the covered raceway ponds are preferably greenhouse covered and are connected in linear succession, wherein there is one covered raceway pond at each stage in the series of covered raceway ponds. In this embodiment, each covered raceway pond is at least 2 times, for example 2 to 5 times, the volume of the covered raceway pond of the previous stage in the series. In a specific embodiment, each covered raceway pond is 2, 3, 4, or 5 times volume of the covered raceway pond of the previous stage in the series. In a preferred embodiment, each covered raceway pond is 5 times volume of the covered raceway pond of the previous stage in the series. In a further specific embodiment, there are at least two stages of open raceway ponds in the series of connected raceway ponds. For example, there may be 2, 3, 4, 5, 6, 7, 8, 9, 10, 15, 20 or 25 stages of open raceway ponds. In one embodiment, there are 2-10 stages of open raceway ponds, 4-6 stages of open raceway ponds, or 5 stages of open raceway ponds. In one specific embodiment, there are more open raceway ponds than closed raceway ponds in the series. In some embodiments, the number of open raceway ponds in each stage is the same for each successive stage in the series. For example, the system 200 in Figure 2A and 2B has 16 ponds in the first stage of covered raceway ponds 210A, 16 ponds in the second stage of covered raceway ponds 210B which are larger than the ponds in the first stage of covered raceway ponds 210A, 16 ponds in the third stage of covered raceway ponds 210C which are larger than the ponds in the second stage of covered raceway ponds 210B. There are also 16 ponds in the first stage of open raceway ponds 210D (fourth stage overall) which are larger than the ponds in the third stage of covered raceway ponds 210C, and 16 ponds in the second stage of open raceway ponds 210E (fifth stage overall), which are larger than the ponds in the first stage of open raceway ponds 210E. Each subsequent pond has at least twice the capacity of the previous pond to hold the entirety of the volume of the previous pond and the equivalent volume of unused seawater. In a particular embodiment, the number of open raceway ponds in each stage increases at each successive stage in the series. In this embodiment, each open raceway pond is connected to two or more open raceway ponds in the next stage in the series, and the collective volume of each of the two or more open raceway pond exceeds the volume of the raceway pond in the preceding stage. Therefore, in this particular embodiment, the algae and water in one open raceway pond is diluted into two or more open raceway ponds when the algae and water are transferred between stages in the series. In a specific embodiment, the number of open raceway ponds in each stage of the series doubles. Therefore, in this embodiment the number of raceway ponds at each stage in the series increases exponentially. For example, the number of open raceway ponds at each stage increases as follows: 1, 2, 4, 8, 16, 32, 64, 128. In this embodiment, as the number of open raceway ponds at each stage increases, so does the volume of each individual raceway pond. In a preferred embodiment, the volume of the individual open raceway ponds in one stage is at least two times, preferably five times, the volume of the individual open raceway ponds in the previous stage. In an alternative embodiment, the volume of the individual open raceway ponds at each stage in the series remains the same, although the collective volume of the raceway ponds increases with each stage as the number of raceway ponds increases. The algae and water may be transferred between raceway ponds in successive stages of the series without any external force, for example it may be transferred under the influence of gravity. However, the algae and water will, on occasion when the local topography does not permit the use of gravity transfers, be pumped from one raceway pond to another, using any suitable pumping means that does not shear the cells. Figure 2A shows a particular layout for a series of connected raceway ponds 210. The advantage of this layout is that it efficiently hugs the coast along the edge of an ocean and enables each raceway pond to have at least one contact with the intake canal 208 and a discharge into the next larger and lower pond. This layout enables the water transfer within the entire pond system to rely on gravity feeds and requires a minimum of piping, while enabling easier maintenance of the ponds. This layout also takes advantage of the frequently encountered natural gradient along coastlines where distance from the shore commonly results in a slight increase in elevation. Discharge phase In some embodiments, the discharging of deacidified water comprises the use of at least one discharge channel. In some embodiments, the at least one discharge channel has a width to depth ratio of greater than 100:1, greater than 90:1, greater than 80:1, greater than 75:1, greater than 70:1, greater than 60:1`, greater than 50:1, greater than 40:1, greater than 30:1, greater than 25:1, greater than 20:1, greater than 10:1, or greater than 5:1. In some embodiments, the length of the at least one discharge channel is more than 1 km, more than 2 km, more than 3 km, more than 4 km, more than 5 km, more than 6 km, more than 7 km, more than 8 km, more than 9 km, more than 10 km, more than 15 km, more than 20 km, more than 25 km, or more than 30 km. In some embodiments, the length of the at least one discharge channel is between 1 km and 30 km. between 1 and 20 km, between 1 and 15 km, between 5 and 30 km, between 5 and 20 km, or between 5 and 15 km. In some embodiments, the length of the at least one discharge channel is at least 1 km, at least 2 km, at least 3 km, at least 4 km, at least 5 km, at least 6 km, at least 7 km, at least 8 km, at least 9 km, at least 10 km, at least 15 km, at least 20 km, at least 25 km, or at least 30 km. In the context of the methods for ocean deacidification of the invention, the smaller the discharge water-air interface in the discharge channel(s), the less carbon dioxide absorption, resulting in a smaller decrease in pH of the discharge water as it progresses through the discharge channel to the ocean. In some embodiments, the discharge water entering the ocean is at least 0.1 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at least 0.2 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at least 0.3 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at least 0.5 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is 0.1-0.5 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is 0.1-0.3 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at pH 8.2-9.0. In some embodiments, the discharge water entering the ocean is at pH 8.2-8.8. In some embodiments, the discharge water entering the ocean is at pH 8.3-8.6. In some embodiments, the discharge water is warmer than the surface water in the ocean (e.g.1-3 °C warmer, such as 2 °C warmer). Advantageously, this results in the discharged water remaining at the surface of the ocean, which facilitates the re-absorption of atmospheric CO2 until equilibrium is reached with the surrounding ocean. In the context of the methods for sequestering carbon dioxide of the invention, longer discharge channels are preferred to facilitate high levels of carbon dioxide absorption by the discharge water while in the discharge channel(s). This results in the pH of the discharge water decreasing approximately to the pH level of the ocean. Accordingly, in some embodiments, the discharge water-air interface has a surface area that is at least 2 km ² . In some embodiments, the discharge water-air interface has a surface area that is at least 5 km ² . In some embodiments, the discharge water-air interface has a surface area that is at least 10 km ² . In some embodiments, the discharge water-air interface has a surface area that is 5-10 km ² . In some embodiments, each of the one or more discharge channels has a volume of at least one million cubic metres. In some embodiments, each of the one or more discharge channels has a volume of at least 2.5 million cubic metres. In some embodiments, each of the one or more discharge channels has a volume of 1-5 million cubic metres. In some embodiments, each of the one or more discharge channels has a length of at least 10 km, at least 25 km, at least 50km or at least 100 km. In some embodiments, each of the one or more discharge channels has a width of 25-250 m (e.g. 50-100 m). In some embodiments, each of the one or more discharge channels has a depth of 0.1-5 m. In some embodiments, each of the one or more discharge channels has a depth of 0.25-1 m. In some embodiments, each of the one or more discharge channels has a depth of 0.4-0.6 m. In some embodiments, the discharge water entering the ocean is at a pH that is no more than 0.2 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at a pH that is no more than 0.1 pH units higher than the pH of the ocean. In some embodiments, the discharge water entering the ocean is at a pH that is the same as the pH of the ocean. In some embodiments, the discharge water entering the ocean is at pH 8.0-8.2. In some embodiments, the discharge water is warmer than the surface water in the ocean (e.g.1-3 °C warmer, such as 2 °C warmer). Advantageously, this results in the discharged water remaining at the surface of the ocean, which facilitates the re-absorption of atmospheric CO2 until equilibrium is reached with the surrounding ocean pH, temperature, salinity and DIC levels In some embodiments, the pH of the land-based mariculture is monitored (e.g. using a pH sensor) during the first algal culture phase. In some embodiments, the pH of the land-based mariculture is monitored (e.g. using a pH sensor) during the second algal culture phase. In some embodiments, the pH of the land-based mariculture is monitored (e.g. using a pH sensor) during the first algal culture phase and the second algal culture phase. In some embodiments, the pH in the first algal culture phase is kept within the range pH 6.5 to pH 7.5. In some embodiments, the pH at the start of the second algal culture phase is within the range pH 6.5 to pH 7.5 (e.g. within the range pH 6.8 to pH 7.2). In some embodiments, the pH at the end of the second algal culture phase is within the range pH 8.4 to pH 10 (e.g. within the range pH 8.4 to pH 9.7). In some embodiments, the pH at the start of the second algal culture phase is within the range pH 6.5 to pH 7.5 (e.g. within the range pH 6.8 to pH 7.2), and the pH at the end of the second algal culture phase is within the range pH 8.4 to pH 9.5 (e.g. within the range pH 8.5 to pH 9.2). In some embodiments, the pH in the first algal culture phase is kept within the range pH 6.5 to pH 7.5, the pH at the start of the second algal culture phase is within the range pH 6.5 to pH 7.5 (e.g. within the range pH 6.8 to pH 7.2), and the pH at the end of the second algal culture phase is within the range pH 8.4 to pH 9.5 (e.g. within the range pH 8.5 to pH 9.2). In some embodiments, the deacidified water discharged in the discharge phase has a pH in the range of pH 8.4 to pH 10 (e.g. within the range pH 8.5 to pH 9.5). In some embodiments, the method is performed at between 10 °C and 35 °C. In some embodiments, the method is performed at between 15 °C and 30 °C. In some embodiments, the salinity of the land-based mariculture is between 20 and 50 per thousand (‰), between 20 and 40 ‰ or between 30 and 40 ‰. In some embodiments, the salinity of the land-based mariculture is more than 20 ‰, more than 25 ‰, more than 30 ‰, more than 35 ‰ or more than 40 ‰. In some embodiments, the salinity of the land-based mariculture is less than 50 ‰, less than 45 ‰, less than 40 ‰, less than 35 ‰, less than 30 ‰ or less than 25 ‰. In some embodiments, the level of dissolved inorganic carbon (DIC) in the land-based mariculture at the start of the first algal culture phase is in the range of 200 μM to 20 mM, such as 500 μM to 5 mM (e.g.1-2.5 mM). In some embodiments, the level of DIC in the land-based mariculture at the start of the second algal culture phase is in the range of 200 μM to 20 mM, such as 500 μM to 5 mM (e.g.1-2.5 mM). In some embodiments, the level of DIC in the land-based mariculture at the end of the second algal culture phase is less than 70% (e.g. less than 50%) of the level of DIC in the land-based mariculture at the start of the second algal culture phase. In some embodiments, the level of DIC in the land-based mariculture at the end of the second algal culture phase is in the range of 100 μM to 10 mM, such as 250 μM to 2.5 mM (e.g.0.5-1.25 mM). In some embodiments, the level of DIC in the land-based mariculture at the start of the second algal culture phase is in the range of 200 μM to 20 mM, such as 500 μM to 5 mM (e.g.1-2.5 mM), and the level of DIC in the land-based mariculture at the end of the second algal culture phase is in the range of 100 μM to 10 mM, such as 250 μM to 2.5 mM (e.g.0.5-1.25 mM). Seed ponds and photobioreactors In one embodiment, the first stage of covered raceway ponds is seeded with algae cultivated in a photobioreactor (PBR) or a seed pond. A PBR achieves a highly controlled environment within the reactor to maintain an uncontaminated stock culture. In order to prevent contamination with competing organisms, bacterial and viral infection, or predatory organisms that reduce the yield or availability of the seed algae, a PBR preferably uses sand and membrane filtered, pre-treated and decontaminated seawater. The exchange of gases is carefully controlled, for example by sparging or bubbling CO2 into the reactor, and removing excess O2. The addition of nutrients and the removal of waste products is also carefully controlled. Preferably, a PBR operates in a sterile environment. A seed pond is an open or closed pond, preferably a closed raceway pond, in which the growth conditions for the algae can be controlled. The seed pond is used to grow a population of algae sufficient to seed the first stage of covered raceway ponds. In one embodiment, the first stage of covered raceway ponds is seeded with algae from a PBR or seed pond in the early morning, e.g. from one hour before to two hours after dawn to enable the algae to exploit their new growth environment, right after they have divided in the predawn hours, for example 1-2 hours before dawn. In a particular embodiment, the first stage of covered raceway ponds is seeded between 1-2 hours before and 1-2 hours after dawn, e.g. between 1 hour before and 2 hours after dawn, or in a specific embodiment when dawn is at 6 AM, the seeding occurs between the hours of 5 AM to 8 AM. In another embodiment, the first stage 210A of covered raceway ponds is seeded with algae cultivated in a photobioreactor (PBR) 204 or a seed pond (not shown). The amount of algae that is used for seeding the initial pond at first stage 210A is referred to as the inoculum density. A PBR 204 achieves a highly controlled environment within the reactor to maintain an uncontaminated stock culture. In order to prevent contamination with competing organisms, bacterial and viral infection, or predatory organisms that reduce the yield or availability of the seed algae, PBR 204 preferably uses sand and membrane filtered, pre-treated and decontaminated seawater. The exchange of gases is carefully controlled, for example by sparging or bubbling air or CO2 into the reactor, and removing excess O2. The addition of nutrients and the removal of waste products is also carefully controlled. Preferably, PBR 204 operates in a clean or sterile environment. A seed pond (not shown) is an open or closed pond, preferably a closed raceway pond, in which the growth conditions for the algae can be controlled. The seed pond is used to grow a population of algae sufficient to seed the first stage 210A of covered raceway ponds. In one embodiment, the first stage 210A of covered raceway ponds is seeded with algae from a PBR 204 or seed pond in the early morning, e.g., from one hour before to two hours after dawn to enable the algae to exploit their new growth environment, right after they have divided in the predawn hours, for example 1-2 hours before dawn. In a particular embodiment, the first stage 210A of covered raceway ponds is seeded between 1-2 hours before and 1-2 hours after dawn, e.g., between 1 hour before and 2 hours after dawn, or in a specific embodiment when dawn is at 6 AM, the seeding occurs between the hours of 5 AM to 8 AM. Algal flow management Algae may be cultivated in seawater, hypersaline water, desalination brine, brackish water, wastewater or freshwater. The choice of water for the culture medium will depend on the algae being grown. Algae will be grown in water that replicates their natural growth environment. Once the seawater has circulated through the series of connected raceway ponds (210), it is cleaned of algae and returned to the warmer ocean surface water, down-current at a distance from the intake to avoid intake of water that has already been used for cultivation of the algae. In one embodiment according to the present invention, algae are first cultivated in at least one stage of covered raceway ponds (210A-210C). The covered raceway ponds (210A-210C) allow for the control of the algae growth environment. The water used to fill the covered raceway ponds (210A-210C) may be filtered or otherwise treated to remove competing and deleterious organisms before being introduced into the covered raceway ponds. In one embodiment, greenhouses (206) are used to cover the raceway ponds (100) and as a result the algae environment is maintained at a higher than ambient temperature. In this embodiment, the temperature within the covered raceway ponds is between 18 °C and 32 °C, for example between 28 °C and 34 °C. This will substantially inactivate organisms acclimated to temperatures of 14°C - 18°C when they are pumped from depth off-shore. Advantageously, covered raceway ponds are less susceptible to contamination, either by bacteria or viruses, or by potentially competing organisms. The relatively controlled environment of the covered raceway pond promotes the algae transitioning into the exponential growth phase. In some embodiments, passive and/or active ventilation may be used in greenhouse (206) to regulate the temperature. As passive ventilation, greenhouse (206) may have walls that have a mesh netting on the inside and are movable outside which can be shut to retain more heat inside the greenhouse (e.g., in winter) or moved to allow free air moment (e.g., in summer). For the active ventilation, if a certain temperature threshold is exceeded, vents turn on to remove heat from greenhouse (206). As the algal cellular density increases, the algae are successively diluted, preferably by being transferred between stages in the series of covered raceway ponds to covered raceway ponds of successively larger volume (e.g., from stage 210A to stage 210B, from stage 210B to 210C). This successive dilution maintains a relatively low cell density of algae, for example between 100,000 cells/ml and 2,000,000 cells/ml, for example about 350,000 cells/ml. Each transfer of the algae to seed a covered raceway pond in the next stage of the series (i.e. the successive dilution of the algae) can be timed to match the growth rate of the algae, or cellular resource requirements. In one embodiment, algae reside in each stage of covered raceway ponds (210A, 210B, 210C) for 2 hours to 10 days, for example 2 hours, 3, hours, 5 hours, 12 hours, 24 hours, 36 hours, 2 days, 3, days or 5 days. In one embodiment, the algae reside in each covered raceway pond (210A, 210B, 210C) for two days, before being transferred to a raceway pond of larger volume. In one embodiment, algae remain in a covered raceway pond (210A, 210B, 210C) for a length of time sufficient for the algae cellular population to at least double, for example 2 hours, 4 hours, 12 hours, 24 hours, 36 hours or 48 hours. In a specific embodiment, algae remain in a covered raceway pond for 24 hours before being transferred to the next stage in the series. Once the algae enter the exponential growth phase, or when sufficient quantities of algae have been cultivated, the algae are transferred to the first stage of open raceway ponds (210D). In one embodiment, the algae and water are transferred in volumes of 1,000 l to 3,000,000 l, for example 360,000 l to 720,000 l, into the first stage of open raceway ponds (210D). The transfer of a relatively large bolus of algae is intended to seed the open raceway ponds to populate the growth environment with a large excess of several orders of magnitude of the product algae relative to any surviving organisms that were within the source water used in the open raceway pond thereby establishing a robust population. The algae may be diluted (e.g. the dilution rate or dilution volume may be increased) by introducing additional water into the current stage of ponds (210A-210E), increasing the volume of water contained within that stage. Additional water may be added by opening the sluice gate of the inlet pipe 108 of a raceway pond 100. Alternatively, the algae may be diluted by transferring the algae to the next stage of ponds and mixing the algae with water already present in those ponds. Algae in an open raceway pond (210D, 210E) are successively diluted by increasing the volume or number of open raceway ponds in each stage of the series (e.g., from stage 210D to 210E). This serial dilution maintains the algae at a low enough cell density to sustain exponential growth. In one embodiment, the algae are successively diluted to maintain a cell density of 50,000 cells/ml to 100,000 cells/ml, for example 200,000 cells/ml to 250,000 cells/ml. This approach is completely different to current methods of cultivating algae in which the algae are grown to artificially high densities often reaching cell densities of over 1 million cells/ml. In one embodiment, algae reside in each stage of raceway ponds for 2 hours to 5 days, for example 2 hours, 3, hours, 5 hours, 12 hours, 24 hours, 36 hours, 2 days, 3, days or 5 days before being transferred to the next stage of raceway ponds in the series. In a specific embodiment, algae remain in a raceway pond for 48 hours before being transferred to the next stage of raceway ponds in the series. In one embodiment, algae remain in a raceway pond for a length of time sufficient for the algae cellular population to at least double, i.e. for one round of cell division to take place. In a specific embodiment, the algae remain in a raceway pond for a length of time sufficient for one, two, three, four or five rounds of cell division to take place. This may be, for example, 2 hours, 4 hours 12 hours, 24 hours, 36 hours, 48 hours, or 72 hours. This successive dilution of algae maintains a low cell density which advantageously maintains the exponential growth phase, thereby increasing productivity. Furthermore, the problems associated with high-density algal culture methods such using traditional raceway ponds and PBRs are avoided. With each successive dilution of the algae, water is added to, and/or is already present in, the covered and open raceway ponds in the next stage in the series. Following the transfer of the algae and water from one stage to seed the next stage in the series, the volume of fluid within each covered and open raceway pond is equal to its capacity. In one embodiment, the entire volume of water in an open and/or covered raceway pond is replaced every 2 hours to 8 days, or every 4 hours to 8 days, preferably every 24 to 72 hours. In a preferred embodiment, the volume of water passing through the series of connected covered and open raceway ponds in 24 hours is greater than 20- 250% of the entire volume of the series of covered and open connected raceway ponds, e.g. greater than 30% of the entire volume of the series of covered and open connected raceway ponds, for example greater than 100% for both seed and growth ponds. This exchange rate of water is much higher than in traditional raceway ponds, where the water replacement rate is usually around 0 – 20% in 24 hours, in order to match the growth rate of the cells and rate of evaporation. This high volume of water exchange has several advantages. In traditional raceway ponds a high cell density of algae is maintained and any contamination can potentially render the entire raceway pond un-harvestable. However, the series of raceway ponds of the present invention is inherently resilient, as small degrees of contamination do not matter since all of the contaminants are inevitably washed out of the series of ponds, and none of the product algae is reintroduced into the series of raceway ponds. In another embodiment, algae reside (i.e., have a residence time) in each stage of open raceway ponds 210D, 210E for 2 hours to 5 days, for example 2 hours, 3, hours, 5 hours, 12 hours, 24 hours, 36 hours, 2 days, 3, days or 5 days before being transferred to the next stage of open raceway ponds in the series (e.g., from stage 210D to 210E). In a specific embodiment, algae remain in a stage of open raceway ponds 210D for 48 hours before being transferred to the next stage of raceway ponds 210E in the series. In one embodiment, algae remain in a stage of an open raceway pond 210D, 210E for a length of time sufficient for the algae cellular population to at least double, i.e., for one round of cell division to take place. In a specific embodiment, the algae remain in a stage of an open raceway pond 210D, 210E for a length of time sufficient for one, two, three, four or five rounds of cell division to take place. This may be, for example, 2 hours, 4 hours 12 hours, 24 hours, 36 hours, 48 hours, or 72 hours. This successive dilution of algae maintains a low cell density which advantageously maintains the exponential growth phase, thereby increasing productivity. Furthermore, the problems associated with high-density algal culture methods such using traditional raceway ponds and PBRs 204 are avoided. With each successive dilution of the algae, water is added to, and/or is already present in, the covered and open raceway ponds in the next stage 210A-210E in the series. Following the transfer of the algae and water from one stage to seed the next stage in the series (e.g., from stage 210A to 210B, from 210B to 210C, from 210C to 210D, from 210D to 210E), the volume of fluid within each raceway pond 100 is equal to the capacity of the raceway pond 100. In one embodiment, the entire volume of water in a raceway pond 100 is replaced every 2 hours to 8 days, or every 4 hours to 8 days, preferably every 24 to 72 hours. In a preferred embodiment, the volume of water passing through the series of connected covered and open raceway ponds 210 in 24 hours is greater than 20-250% of the entire volume of the series of covered and open connected raceway ponds 210, e.g., greater than 30% of the entire volume of the series of covered and open connected raceway ponds, for example greater than 100% for both seed and growth ponds. This exchange rate of water is much higher than in traditional raceway ponds, where the water replacement rate is usually around 0 – 20% in 24 hours, in order to match the growth rate of the cells and rate of evaporation. This high volume of water exchange has several advantages. In traditional raceway ponds a high cell density of algae is maintained and any contamination can potentially render the entire raceway pond un-harvestable. However, the series of raceway ponds 210 is inherently resilient, as small degrees of contamination do not matter since all of the contaminants are inevitably washed out of the series of ponds, and none of the product algae is reintroduced into the series of raceway ponds. Harvesting the algae In one embodiment, the method of the invention further comprises the step of harvesting the algae. Harvesting of the algae in a raceway pond may be performed once algal growth rate falls below a predetermined threshold. In general, it is desirable to reduce nutrient supplementation rate in the final ponds of a series of raceway ponds, to force the cells down to a metabolic path where they have a higher carbon to nitrogen ratio and carbon content, and to avoid excess nutrients being washed out of the system (e.g., system 200). However, if the algal growth rate falls below the predetermined threshold (e.g., stops growing), then harvest should be performed as soon as possible. Alternatively, harvesting of the algae in a raceway pond may be performed once the biomass in the raceway pond has exceeded a predetermined threshold. In such embodiments, the predetermined threshold may be set based on the maximum biomass that the raceway pond is capable of holding. For example, the predetermined threshold may be set to at least 70%, 75%, 80%, 85%, 90%, or 95% of the maximum biomass that the raceway pond is capable of holding. In some embodiments, the algae are harvested by tangential flow filtration. In some such embodiments, the tangential flow filtration is performed using filters comprising hydrophilic simple weave (irradiated) polyester fabric. In some embodiments, the algae are harvested by filtering with a rotary mesh screen. In some such embodiments, the screen comprises a (pore-sized) mesh and a filter comprising hydrophilic (irradiated) polyester fabric. In some embodiments, algae are cultured. In some such embodiments, the algae are harvested by tangential flow filtration. In some such embodiments, the tangential flow filtration is performed using filters comprising hydrophilic (irradiated) polyester fabric. In some embodiments, algae are cultured. In some such embodiments, the algae are harvested by filtering with a rotary mesh screen. In some such embodiments, the screen comprises a (pore-sized) mesh and a filter comprising hydrophilic (irradiated) polyester fabric. In some embodiments, algae are cultured and the algae are harvested by tangential flow filtration. In some such embodiments, the tangential flow filtration is performed using filters comprising hydrophilic (irradiated) polyester fabric. In some embodiments, algae are cultured and the algae are harvested by filtering with a rotary mesh screen. In some such embodiments, the screen comprises a (pore-sized) mesh and a filter comprising hydrophilic (irradiated) polyester fabric. In some embodiments, diazotrophic phytoplankton that are chain-forming cyanobacteria, such as Trichodesmium sp. (e.g. Trichodesmium erythraeum), are cultured. In some such embodiments, the cyanobacteria are harvested by tangential flow filtration. In some such embodiments, the tangential flow filtration is performed using filters comprising hydrophilic (irradiated) polyester fabric. In some embodiments, diazotrophic phytoplankton that are chain-forming cyanobacteria, such as Trichodesmium sp. (e.g. Trichodesmium erythraeum), are cultured. In some such embodiments, the cyanobacteria are harvested by filtering with a rotary mesh screen. In some such embodiments, the screen comprises a (pore-sized) mesh and a filter comprising hydrophilic (irradiated) polyester fabric. In some embodiments, DDAs comprising a chain-forming diatom (e.g. Hemiaulus sp.) are cultured and the algae are harvested by tangential flow filtration. In some such embodiments, the tangential flow filtration is performed using filters comprising hydrophilic (irradiated) polyester fabric. In some embodiments, DDAs comprising a chain-forming diatom (e.g. Hemiaulus sp.) are cultured and the algae are harvested by filtering with a rotary mesh screen. In some such embodiments, the screen comprises a (pore-sized) mesh and a filter comprising hydrophilic (irradiated) polyester fabric. Suitable rotary mesh screens include (simple weave) polyester screens that have a pore size of 10-200 µM, preferably a pore size of 20-120 µM. In some embodiments, these screens have been irradiated. Advantageously, this makes the screen more hydrophilic, which improves the filtration rate. Suitable rotary mesh screens may comprise a surfactant coating, such as SAATIcare Hyphyl ^TM . A further example of a suitable rotary mesh screens is monofilament polyester fabric, such as SUPREX (EXTRIS). In the context of rotary mesh screens, the thinner the fibre strands, the larger the percentage of open area for filtration, which the inventors have found to be advantageous for harvest filtration of algae. Accordingly, in some embodiments, the average fibre strand diameter in a rotary mesh screen less than 50 µM. Accordingly, in some embodiments, the rotary mesh screens have a pore size of 10-200 µM and an average fibre strand diameter of less than 50 µM. Accordingly, in some embodiments, the rotary mesh screens have a pore size of 20-120 µM and an average fibre strand diameter of less than 50 µM. In some embodiments, the harvested algal slurry (or algal concentrate) is highly concentrated. In some embodiments, the harvested algal slurry (or algal concentrate) is between 1% and 10% dry weight. In some embodiments, the harvested algal slurry (or algal concentrate) is between 2% and 9% dry weight. In some embodiments, the harvested algal slurry (or algal concentrate) is between 3% and 7% dry weight. In some embodiments, the harvested algal slurry (or algal concentrate) is between 4% and 6% dry weight. In some embodiments, the harvested algal slurry (or algal concentrate) is solar dried and buried to sequester carbon in the ground. The drying and burial of harvested algae is discussed in more detail in International Patent Application No. PCT/GB2023/051392, incorporated herein by reference. Maintenance of the raceway ponds In one embodiment, the method of the invention further comprises the step of maintaining the raceway ponds. Maintenance may be performed upon detection of a contaminant in a raceway pond. Contaminants may be present in the environment surrounding the raceway pond, especially arising from environmental perturbations such as rainfall or sandstorms. When the raceway pond is situated in a desert, the most common contaminant is sand. Additionally or alternatively, the contaminant may be present oceanic contaminants coming in with fresh seawater. The methods of the invention that comprise culturing algae in a series of connected raceway ponds typically produce sequential batches of algae as opposed to the steady state continuous harvesting of algae that is traditionally utilised in algal culture. This means that batches of algae can be separated according to need. For example, as the algae pass through the series of connected ponds, trace contamination from the air or other sources may occur, particularly in the open raceway ponds (100). However, the series of connected raceway ponds of the present invention is inherently resilient, because small degrees of contamination do not matter as none of the product algae is reintroduced and all of the contaminants are eventually washed out of the system (200). Furthermore, in one embodiment the dilution of the algae through the repeat addition of seawater also dilutes any contaminants present. Raceway ponds in the series are connected to allow algae and water to flow from one raceway pond to another, but each pond can be isolated when required. This is particularly useful to allow the ponds to be cleaned to remove sediment or biofilms. Therefore, between batches of algae in different raceway ponds, where algae are transferred every 2, 3, 4, 5, 6, 8, 10, 12, 24, 36 hours, 2 days, 3 days, 5 days apart, a cleaning shift can be introduced wherein each raceway pond in the series is sequentially pumped dry, cleaned, for example with truck-mounted rotating brushes, and flushed with water. A cleaning cycle can be performed once a month, and every several cleaning cycles an extra day may be introduced to add a day for drying the ponds. Equipment can be cleaned with 0.0001-0.01% peroxyacetic acid or similar disinfectants such as hypochloric acid before it is seeded with algae from the raceway pond in the preceding stage in the series, and topped up with fresh water. In this manner, a running cleaning wave can travel through the entire series of connected covered and open raceway ponds (and the harvesting ponds if desired). This may be scheduled according to the prevalence of oceanic contaminants coming in with the fresh seawater or environmental perturbations such as rainfall or sandstorms. In some embodiments, equipment is cleaned with sodium hypochlorite before it is seeded with algae from the raceway pond in the preceding stage in the series, and topped up with fresh water. Exemplary methods In one embodiment, the invention provides a method for ocean deacidification, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, wherein the one or more nutrient acids comprise nitric acid (HNO3), phosphoric acid (H3PO4) and orthosilicic acid (H4SiO4), wherein HNO3 is added in the first algal culture phase to a final concentration of 8-800 μM, wherein H3PO4 is added in the first algal culture phase to a final concentration of 0.15-15 μM, and wherein H4SiO4 is added in the first algal culture phase to a final concentration of between 0.3 μM and 5.0 μM, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4 and (c) a discharge phase, wherein the discharge phase comprises discharging de-acidified water obtained from step (b) into the ocean, wherein the land-based mariculture is carried out in a connected series of raceway ponds, and wherein the method further comprises harvesting the algae, and wherein the algae are diatoms. In one embodiment, the invention provides a method for ocean deacidification, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, wherein the one or more nutrient acids comprise nitric acid (HNO ₃ ) and phosphoric acid (H ₃ PO ₄ ), wherein HNO ₃ is added in the first algal culture phase to a final concentration of 8-800 μM, and wherein H ₃ PO ₄ is added in the first algal culture phase to a final concentration of 0.15-15 μM, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4 and (c) a discharge phase, wherein the discharge phase comprises discharging de-acidified water obtained from step (b) into the ocean, wherein the land-based mariculture is carried out in a connected series of raceway ponds, and wherein the method further comprises harvesting the algae, and wherein the algae are bloom-forming cynaobacteria. In one embodiment, the invention provides a method for ocean deacidification, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, wherein the one or more nutrient acids comprise phosphoric acid (H3PO4), wherein H ₃ PO ₄ is added in the first algal culture phase to a final concentration of 0.15-15 μM, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4 and (c) a discharge phase, wherein the discharge phase comprises discharging de-acidified water obtained from step (b) into the ocean, wherein the land-based mariculture is carried out in a connected series of raceway ponds, and wherein the method further comprises harvesting the algae, and wherein the algae are diazotrophic phytoplankton. In one embodiment, the invention provides a method for ocean deacidification, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, wherein the one or more nutrient acids comprise phosphoric acid (H3PO4) and orthosilicic acid (H4SiO4), wherein H3PO4 is added in the first algal culture phase to a final concentration of 0.15-15 μM, and wherein H4SiO4 is added in the first algal culture phase to a final concentration of between 0.3 μM and 5.0 μM, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4 and (c) a discharge phase, wherein the discharge phase comprises discharging de-acidified water obtained from step (b) into the ocean, wherein the land-based mariculture is carried out in a connected series of raceway ponds, and wherein the method further comprises harvesting the algae, and wherein the algae are diazotroph-diatom assemblages. In one embodiment, the invention provides a method for sequestering carbon dioxide from the atmosphere, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, wherein the one or more nutrient acids comprise nitric acid (HNO ₃ ), phosphoric acid (H ₃ PO ₄ ) and orthosilicic acid (H ₄ SiO ₄ ), wherein HNO ₃ is added in the first algal culture phase to a final concentration of 8-800 μM, wherein H ₃ PO ₄ is added in the first algal culture phase to a final concentration of 0.15-15 μM, and wherein H ₄ SiO ₄ is added in the first algal culture phase to a final concentration of between 0.3 μM and 5.0 μM, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4, wherein the discharge water-air interface has a surface area that is at least 1 km ² , wherein the discharge water entering the ocean is at a pH that is no more than 0.3 pH units higher than the pH of the ocean, and (c) a discharge phase, wherein the discharge phase comprises discharging ‘de-acidified’ water obtained from step (b) into the ocean, wherein the land-based mariculture is carried out in a connected series of raceway ponds, and wherein the method further comprises harvesting the algae, and wherein the algae are diatoms. In one embodiment, the invention provides a method for sequestering carbon dioxide from the atmosphere, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, wherein the one or more nutrient acids comprise nitric acid (HNO ₃ ) and phosphoric acid (H ₃ PO ₄ ), wherein HNO ₃ is added in the first algal culture phase to a final concentration of 8-800 μM, and wherein H ₃ PO ₄ is added in the first algal culture phase to a final concentration of 0.15-15 μM, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4, wherein the discharge water-air interface has a surface area that is at least 1 km ² , wherein the discharge water entering the ocean is at a pH that is no more than 0.3 pH units higher than the pH of the ocean, and (c) a discharge phase, wherein the discharge phase comprises discharging ‘de-acidified’ water obtained from step (b) into the ocean, wherein the land-based mariculture is carried out in a connected series of raceway ponds, and wherein the method further comprises harvesting the algae, and wherein the algae are bloom-forming cynaobacteria. In one embodiment, the invention provides a method for sequestering carbon dioxide from the atmosphere, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, wherein the one or more nutrient acids comprise phosphoric acid (H3PO4), wherein H3PO4 is added in the first algal culture phase to a final concentration of 0.15-15 μM, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4, wherein the discharge water-air interface has a surface area that is at least 1 km ² , wherein the discharge water entering the ocean is at a pH that is no more than 0.3 pH units higher than the pH of the ocean, and (c) a discharge phase, wherein the discharge phase comprises discharging ‘de-acidified’ water obtained from step (b) into the ocean, wherein the land-based mariculture is carried out in a connected series of raceway ponds, and wherein the method further comprises harvesting the algae, and wherein the algae are diazotrophic phytoplankton. In one embodiment, the invention provides a method for sequestering carbon dioxide from the atmosphere, wherein the method comprises: (a) a first algal culture phase, wherein the first algal culture phase comprises culturing algae in land-based mariculture, and wherein one or more nutrient mineral acids are added during culturing, wherein the one or more nutrient acids comprise phosphoric acid (H3PO4) and orthosilicic acid (H4SiO4), wherein H3PO4 is added in the first algal culture phase to a final concentration of 0.15-15 μM, and wherein H4SiO4 is added in the first algal culture phase to a final concentration of between 0.3 μM and 5.0 μM, (b) a second algal culture phase, wherein the second algal culture phase comprises culturing the algae in land-based mariculture without nutrient addition, such that the pH in the mariculture increases to at least pH 8.4, wherein the discharge water-air interface has a surface area that is at least 1 km ² , wherein the discharge water entering the ocean is at a pH that is no more than 0.3 pH units higher than the pH of the ocean, and (c) a discharge phase, wherein the discharge phase comprises discharging ‘de-acidified’ water obtained from step (b) into the ocean, wherein the land-based mariculture is carried out in a connected series of raceway ponds, and wherein the method further comprises harvesting the algae, and wherein the algae are diazotroph-diatom assemblages. General The term “comprising” encompasses “including” as well as “consisting” e.g. a composition “comprising” X may consist exclusively of X or may include something additional e.g. X + Y. The term “about” in relation to a numerical value x is optional and means, for example, x+10%. The various steps of the methods may be carried out by the same or different people or entities. The various steps of the methods may be carried out at the same time or at different times, in the same geographical location or in different geographical locations, e.g. countries, and by the same or different people of entities. EXAMPLES Various aspects and embodiments of the invention are described below in more detail by way of example. It will be appreciated that modification of detail may be made without departing from the scope of the invention. Example 1 This example provides a direct comparison of the pH of pond seawater with no supplementation, nutrient supplementation, and nutrient acid supplementation at three timepoints throughout the land- based mariculture method described herein. In this example, Skeletonema pseudocostatum was used as an exemplary algal species. The results are shown in Figure 3. Nutrient acid supplementation initially lowers the pH of the pond seawater, but ultimately leads to greater deacidification of the pond seawater than is seen when algae are cultured with equivalent concentrations of mineral nutrient supplements (NaNO ₃ , NaH ₂ PO ₄ and NaSiO(OH) ₃ ) or without nutrient supplementation. Without wishing to be bound by any theory, the deacidification occurs primarily through the efficient uptake of bicarbonate and H+ ions by the algae. Example 2 This example provides a direct comparison of the dissolved inorganic carbon (DIC) of pond seawater with no supplementation, nutrient supplementation, and nutrient acid supplementation at three timepoints throughout the land-based mariculture method described herein. In this example, Skeletonema pseudocostatum was used as an exemplary algal species. The results are shown in Figure 4. Advantageously, supplementation with nutrient mineral acids results in more efficient removal of DIC from pond seawater than is observed following the addition of equivalent concentrations of mineral nutrients (NaNO ₃ , NaH ₂ PO ₄ and NaSiO(OH) ₃ ) or with no supplementation. This greater efficiency translated into an improved rate of algal biomass production. In particular, the dry weight of algal biomass produced per day was ~30% higher with nutrient acid supplementation than with nutrient supplementation. REFERENCES AR6: https://www.ipcc.ch/report/sixth-assessment-report-cycle Benemann, J.R. & Oswald, W.J. Systems and Economic Analysis of Microalgae Ponds for Conversion of CO2 to Biomass. Final Report to the Pittsburgh Energy Technology Center (1996) Furukawa, T., Watanaba, M. and Shihira-Ishikawa, I. Green and blue-light-mediated chloroplast migration in the centric diatom Pleurosira laevis Protoplasma, 203;214-220 (1998) Hilton J.A., Ecology and Evolution of Diatom Associated Cyanobacteria through genetic analysis, June 2014, PhD Dissertation, UC Santa Cruz Kraml, M. and Herrmann, H. Red–blue interaction in Mesotaenium chloroplast movement—blue seems to stabilize the transient memory of the phytochrome signal. Photochem. Photobiol., 53:255– 259 (1991) Kusmayadi, A., Suyono E. A., Nagarajan, D., Chang, J.-S. and Yen, H.W., Application of computational fluid dynamics (CFD) on the raceway design for the cultivation of microalgae: a review, 2020, Journal of Industrial Microbiology and Biotechnology, 47(4-5):373–382. Mutalipassi M., Riccio G., Mazzella V., Galasso C., Somma E., Chiarore A., de Pascale D. and Zupo V., Symbioses of Cyanobacteria in Marine Environments: Ecological Insights and Biotechnological Perspectives, 2021, Mar. Drugs 19:227-256 Tuo S-H., Lee Chen Y-L., Chen H-Y., Chen T-Y., Free-living heterocystous cyanobacteria in the tropical marginal seas of the western North Pacific, 2017, J. Plankton Res.39(3):404–422 Weissman, J.C. and Goebel, R.P. Design and Analysis of Pond Systems for the Purpose of Producing Fuels. Solar Energy Research Institute, Golden Colorado (1987)