BACKGROUND

[0001 ] Hydrocarbon-producing wells are often stimulated by hydraulic fracturing operations, wherein proppants may be used to hold open or "prop" open fractures created during high-pressure pumping. Once the pumping-induced pressure is removed, proppants may prop open fractures in the rock formation and thus precl ude the fracture from closing. As a result, the amount of formation surface area exposed to the well bore is increased, enhancing hydrocarbon recovery rates.

[0002] In some examples, a hydraulic fracturing operation may comprise pumping a hydraulic fracturing fluid comprising a carrier fluid and a proppant through a wellbore into a subterranean formation. The high pressure may cause the formation to fracture and may al low the fracturing fluid to enter the fractures created in the formation. In some instances, it may be advantageous to use a micro-proppant to prop open micro-fractures created in the formation. The micro-proppant may aid in additional hydrocarbon recovery by propping open smal l fractures not accessible by larger-sized proppants. A fracturing fluid comprising a micro- proppant and a large-size proppant may expose more formation surface area to the wellbore than fracturing solely with large-size proppant.

[0003] While micro-proppants may allow access to natural and micro-factures which are not accessible by using larger-sized proppant, the use of micro-proppants may present some challenges. By way of example, the micro-proppants may undesirably flocculate and fal l out of solution. The micro-proppants may comprise a charged surface which may unfavorably interact with other micro-proppant particles or additives in the fracturing fluid. For example a fracturing fluid may comprise a carrier fluid, a micro-proppant w ith a negative surface charge, and a friction reducer with a positive surface charge. M icro-proppants may be provided in a dispersion. The opposite charges of the micro-proppant and friction reducer may cause the micro-proppant dispersion to become unstable and may cause the micro-proppant to flocculate and settle out of the fracturing fl uid. Examples of other factors that may influence micro- proppant dispersion stabi l ity in a fracturi ng fluid include the net surface charge of the micro- proppant and additives, polymer charge density and molecular weight (polymer bridging), concentration of ions in sol ution (electrostatic screening), mi cro-proppant concentration, temperature, and carrier fluid rheology, among others. BRIEF DESCRIPTION OF THE DRAWINGS

[0004] These drawings illustrate certain aspects of the present disclosure, and should not be used to l imit or define the disclosure.

[0005] The FIGURE is a schematic view of a wel l system utilized for hydraul ic fracturing.

DETAILED DESCRIPTION

[0006] The systems, methods, and/or compositions disclosed herein may relate to subterranean operations and, in some systems, methods, and compositions, to introduction of a treatment fl uid, such as a fracturi ng fl uid, into a subterranean formation penetrated by a wel lbore. In particular, a fracturing fluid may comprise a carrier fluid, concentrated proppant slurry, and optional additives. The formation treatment may be performed in an initial fracturi ng operation, or during a re-fracturing operation after an initial fracturi ng operation has been performed on the subterranean zone.

[0007] Examples of carrier fluids may include, without l imitation, aqueous fluids, non-aqueous fluids, slickwater fl uids, aqueous gels, viscoelastic surfactant gels, foamed gels, and emulsions, for example. Examples of suitable aqueous fluids may include fresh water, saltwater, brine, seawater, and/or any other aqueous fluid that may not undesirably interact with the other components used in accordance with the present disclosure or with the subterranean formation. Examples of suitable non-aqueous fluids may include organic liquids, such as hydrocarbons (e.g. , kerosene, xylene, tol uene, or diesel), oils (e.g., mineral oi ls or synthetic oil s), esters, and any combi nation thereof. Suitable sl ickwater fluids may general ly be prepared by addition of smal l concentrations of polymers to water to produce what is known in the art as "slick-water." Suitable aqueous gels may generally comprise an aqueous fluid and one or more gelling agents. Suitable emul sions may be comprised of two immiscible l iquids such as an aqueous fl uid or gel led fluid and a hydrocarbon. Foams may be created by the addition of a gas, such as carbon dioxide or nitrogen. Additional ly, the carrier fluid may be an aqueous gel comprised of an aqueous fl uid, a gel l ing agent for gell ing the aqueous fluid and i ncreasi ng its viscosity, and, optional ly, a crossl i nki ng agent for crossl inki ng the gel and further increasi ng the viscosity of the fl uid. The i ncreased viscosity of the gel led, or gel led and crosslinked, treatment fl uid, inter al ia, may reduce fl uid loss and may al low the carrier fluid transport sign ificant quantities of suspended particulates. The density of the carrier fl uid may be increased to provide add itional particle transport and suspension i n some appl ications. [0008] The concentrated proppant slurry may comprise a slurry fluid, proppant, and one or more additives. The slurry fluid may be any fluid suitable for use in a fracturing fluid. The fluid should be compatible with the subterranean formation and any other fluids or additives in the fracturing fluid. Without l imitation the slurry fluid may comprise water or l iquid hydrocarbons.

[0009] The concentrated proppant sl urry may comprise a proppant. Proppants may comprise a particle size from about 0.01 m icron to about 500 microns, about 0.1 micron to about 1 00 microns, about 1 00 microns to about 200 microns, about 200 microns to about 300 microns, about 300 microns to about 400 microns, about 400 microns to about 500 microns, about 1 micron to about 250 microns, or about 250 microns to about 500 microns. In some examples, the proppant may be considered a micro-proppant. As used herein, the term "micro- proppant" refers to proppant having a particle size of less than about 1 50 microns. Proppants may comprise any suitable material . In general proppants should have a crush strength higher than the fracture gradient of the formation so as to avoid crushing the proppant. Proppants should also be resistant to chemical attack from chemicals present in the subterranean formation and from chemicals added to the fracturing fluid. Some suitable proppants without limitation may incl ude silica sand, calcium carbonate sand, resin coated sand, ceramic proppants, fly ash, and si ntered bauxite. An example of a commercial proppant suitable for use is MONOPROP® Lightweight Proppant available from Halliburton Energy Services Inc. Proppants may comprise any density . In some examples, proppants may be classified as l ightweight or lo density and may have a density of about 1 .25 to about 2.2 g/cm ³ . Using a low density proppant may have several advantages including but not limited to increased conductivity, easier placing with low viscosity fluids, and more uniform distribution within a fracture. Proppants may comprise any shape, includ ing but not l i mited, to spherical, toroidal, amorphous, planar, cubic, or cyl indrical . Proppants may further comprise any roundness and sphericity. Proppant may be present in any concentration or loadi ng. Without l imitation, the proppant may be present in an amount o f about 1 pounds per gal lon ("l b/gal") to about 20 l b/gal, about 1 lb/gal to about 5 l b/gal . about 5 lb/ gal to about 1 0 l b/gal , about 10 lb/gal to about 1 5 lb/gal, about 1 5 lb/gal to about 20 lb/gal. about 1 lb/gal to about 10 lb/gal, or about 1 0 lb/gal to about 20 lb/gal . With the benefit of this disclosure, one of ord inary skill i n the art should be able to select an appropriate proppant and loading.

[00 1 0] The concentrated proppant sl urry may comprise one or more additives. In some exampl es, the additive may comprise a dispersing agent. Dispersing agents may comprise any chemical that disrupts the surface i nteractions of proppant and potential flocculating agents in the fracturing fluid. Some examples of dispersants without l imitation may incl ude aminosilanes, acacia gum, acrylamide copolymer, acrylate copolymers and their ammonium salts, acryl ic acid homopolymer, 2-acrylamido-2-methylpropane sulfonic acid copolymer, carboxylate and sulfonate copolymer, coglycerides, d icaprylyl carbonate, maleic anhydride, phosphinocarboxylic acid, polyacrylic acid, propylheptyl caprylate. sodium acrylate homopolymer, and sodium nitrite. Additional additives may include, but are not limited to, surfactants, friction reducers, l ubricants, and consolidating agents. The additives may be present in any concentration. Without l i mitation, the additives, including the dispersing agents, may be present in an amount of about 1 to about 50 gallons per thousand (G PT), about 1 to about 1 0 GPT, about 10 to about 20 GPT, about 20 to about 30 G PT, about 30 to about 40 GPT. about 40 to about 50 GPT. about 1 to about 25 GPT. or about 25 to about 50 GPT. GPT refers to gal lons of additive per thousand gal lons of fl uid the additi ve is placed in. One of ordinary ski ll in the art, with the benefit of this disclosure, should be able to select appropriate additives and concentrations for a particular application.

[001 1 ] The proppant may comprise an electrical ly charged surface. In some examples. the proppant surface charge may be negative or anionic. Some fracturing fluid additives may comprise surface charges that are opposite of the proppant. In some examples, clay control agents and friction reduci ng agents may comprise positive surface charges. In solution, the particles of opposite charges may interact which may cause the proppant to flocculate and fall out of solution. The addition of a dispersing agent may reduce the interactions between the opposite-charged mol ecules thereby reducing or el iminating the flocculating of proppant.

[0012] In some examples, the concentrated proppant slurry may be pre-mixed and del ivered to the well site. This may have some advantages over mixing concentrated proppant slurry on the fly at the wel l site including, but not l i mited to, mi nimized dust and less equipment on site. The concentrated proppant slurry may be del ivered by chemical tote, barrel, or any other means. In another exampl e, the concentrated proppant sl urry is made on site and mixed with the carrier fl uid and optional additives on the fly. The concentrated proppant slurry may also be stored for later use. The concentrated proppant sl urry may be di l uted and combined with a carrier fl uid and optional add iti ves to form the fracturing fl uid. The final physical properties of the fracturing fl uid such as viscosity and density will depend on the relative amounts of carrier fl uid, proppant. and optional additives. Without l imitation the viscosity may be about 3 cP to about 20 cP. about 3 cP to about 10 cP, or about 10 cP to about 20 cP. One of ordinary skil l i n the art, with the benefit of this disclosure, should be able to select appropriate additives and concentrations for a particular application. The fracturing treatment fluid may also be com bi ned with other subterranean treatments which may incl ude. w ithout l i mitation, matrix acidizing and fracture acidizi ng. [001 3] The fracturing fluid may comprise any number of optional additives, including, but not limited to, salts, acids, fluid loss control additives, gas, foamers, corrosion inhibitors, scale inhibitors, catalysts, clay control agents, biocides. friction reducers, iron control agent, antifoam agents, bridgi ng agents, dispersants, hydrogen sulfide ("H2S") scavengers, carbon dioxide ( "CO ₂ ") scavengers, oxygen scavengers, l ubricants, viscosifiers, breakers, weighting agents, inert sol ids, emulsifiers, emulsion thinner, emulsion thickener, surfactants, lost circulation additives, pH control additive, buffers, crosslinkers, stabi lizers, chelating agents, mutual solvent, oxid izers, reducers, consol idating agent, complexing agent, particulate materials and any combination thereof. With the benefit of this disclosure, one of ordinary skil l in the art should be able to recognize and select a suitable optional additive for use in the fracturing fluid.

[00 14] In certain systems, methods, and/or compositions of the present disclosure, a friction reducer may be used. The friction reducer may be incl uded in the fracturing fluid to form a sl ickwater fluid, for example. The friction reducing polymer may be a synthetic polymer. Additionally, for example, the friction reducing polymer may be an anionic polymer or a cationic polymer. By way of example, suitable synthetic polymers may comprise any of a variety of monomeric units, incl uding acrylamide, acryl ic acid, 2-acrylamido-2- methylpropane sulfonic acid, N,N-dimethyIacrylamide, vinyl sulfonic acid, N-vinyl acetamide, N-vinyl formamide, itaconic acid, methacrylic acid, acrylic acid esters, methacrylic acid esters and combinations thereof

[001 5] Suitable friction reducing polymers may be in an acid form or in a salt form. As wi ll be appreciated, a variety of salts may be prepared, for example, by neutralizing the acid form of the acryl ic acid monomer or the 2-acrylamido-2-methylpropane sulfonic acid monomer. In addition, the acid form of the polymer may be neutralized by ions present in the fracturing fluid. The term "polymer" in the context of a friction reducing polymer, may be intended to refer to the aci d form of the friction reducing polymer, as wel l as its various salts.

[001 6] The friclion reducing polymer may be included in the fracturi ng fl uid, for example, in an amount of about 0.5 to about 1 0 G PT, about 0.5 to about 5 GPT, or about 5 to about 1 0 GPT. The friction reduci ng polymers may be included i n the fracturing fluid in an amount sufficient to reduce friction without gel formation upon mixing. By way of example, the fracturing fl uid comprising the friction reducing polymer may not exhibit an apparent yield point. Whi le the add ition of a friction reducing polymer may mi ni mal ly increase the viscosity of the fracturing fl uid, the polymers may general ly not be incl uded i n the example fracturi ng fluid i n an amount su ffi cient to substantially increase the viscosity. For example, when proppant is included i n t he fracturing fl uid, velocity rather than fluid viscosity general ly may be rel ied on for proppant transport. Additional ly, the friction reducing polymer may be present in an amount in the range from about 0.01 % to about 0.1 5% by weight of the carrier fluid. Alternatively, the friction reducing polymer may be present in an amount in the range from about 0.025% to about 0.1 % by weight of the carrier fluid.

[001 7] A method may comprise providing a concentrated proppant slurry comprising a sl urry fluid and a proppant; preparing a fracturing fluid by combining components comprisi ng the concentrated proppant slurry, a carrier fluid, and a dispersing agent; and introducing the fracturing fluid through a wel lbore penetrating a subterranean formation at an injection rate and pressure that is at or above the fracture gradient of the subterranean formation. This method may include any of the various features of the compositions, methods, and systems disclosed herein, including one or more of the following features in any combination. The method may also comprise i ntroducing the fracturing fl uid in to the subterranean formation after at least one primary fracture has been generated in the subterranean formation. The proppant may have a particle size of about 0.01 micron to about 500 microns. The proppant may comprise a micro-proppant wherein the micro-proppant has a particle size of about 1 micron to about 1 50 microns. The proppant may be present in the concentrated proppant slurry in a concentration of about 10 lb/gal to about 20 lb/gal. The dispersing agent may be a component of the concentrated proppant sl urry. The dispersing agent may comprise at least one dispersing agent selected from the group consisting of aminosilanes, acacia gum, acrylam ide copolymer, aery I ate copolymers and their ammonium salts, acrylic acid homopolymer, 2-acrylamido-2-methylpropane sulfonic acid copolymer, carboxylate and sulfonate copolymer, coglycerides, dicaprylyl carbonate, maleic anhydride, phosphinocarboxyl ic acid, polyacryl ic acid, propylheptyl caprylate, si licon dioxide, sodium acrylate homopolymer. and sodi um nitrite. The carrier fluid may be a sl ickwater fl uid wherein the sl ickwater fl uid comprises an aqueous fl uid and friction reducing polymer. The sl urry fluid may comprise an aq ueous fluid. The proppant may comprise at least one particulate selected from the group consisting of si l ica sand, calci um carbonate sand, resin coated sand, ceramic, fly ash. and sintered bauxite. The proppant slurry may be pre-mixed before combini ng the carrier fl uid and the dispersing agent.

[001 8] A concentrated proppant sl urry may comprise a slurry fl uid, a proppant in a concentration of about 1 l b/gal to about 20 lb/gal, and a dispersing agent. This concentrated proppant sl urry may i nclude any of the various features of the compositions, methods, and systems disclosed herei n, including one or more of the fol lowing features in any combination. The proppant may further be present in a concentration of about 10 lb/gal to about 20 lb/gal . The proppant may have a particle size of about 0.01 m icron to about 500 microns. The proppant may be a micro-proppant having a particle size of about 1 micron to about 1 50 microns. The proppant may comprise at least one particulate selected from the group consisting of sil ica sand, calcium carbonate sand, resin coated sand, ceramic, fly ash, and sintered bauxite. The dispersi ng agent may comprise at least one dispersing agent selected from the group consisting of aminosi lanes, acacia gum, acrylamide copolymer, acrylate copolymers and their ammonium salts, acrylic acid homopolymer, 2-acrylamido-2-methylpropane sulfonic acid copolymer, carboxylate and sulfonate copolymer, coglycerides. dicaprylyl carbonate, maleic anhydride, phosphi nocarboxyl ic acid, polyacryl ic acid, propylheptyl caprylate, silicon dioxide, sodium acrylate homopolymer, and sodium nitrite. The slurry fl uid may comprise an aqueous fluid.

[001 9] A system may comprise a dispersing agent; a concentrated proppant slurry comprising a slurry fl uid and a proppant; a carrier fluid; mixing equipment operable to mix a fracturi ng fl uid comprisi ng the dispersing agent, the concentrated proppant sl urry, and the carrier fluid; and pumpi ng equipment operable to deliver the fracturing fluid into a subterranean formation at or above a fracture gradient of the subterranean formation. This system may incl ude any of the various features of the compositions, methods, and systems disclosed herein, i ncl uding one or more of the fol lowing features in any combination. The proppant may have a particle size of about 0.01 micron to about 500 microns. The proppant may comprise a micro-proppant wherein the micro-proppant has a particle size of about 1 micron to about 1 50 microns. The proppant may be present in the concentrated proppant slurry in a concentration of about 1 0 lb/gal to about 20 lb/gal dispersing agent may be present in the concentrated proppant slurry. The dispersing agent may comprise at least one dispersing agent selected from the group consisting of aminosi lanes, acacia gum, acrylamide copolymer, acrylate copolymers and their ammoni um salts, acryl ic acid homopolymer, 2-acrylamido-2- methylpropane sul fonic acid copolymer, carboxylate and sulfonate copolymer, coglycerides, dicaprylyl carbonate, maleic anhydride, phosphinocarboxyl ic acid, polyacryl ic acid, propyl heptyl capryl ate. si l icon dioxide, sodium acrylate homopolymer, and sodium nitrite. The carrier fl uid may be a s! ickwater fl uid wherein the slickwatcr fluid comprises an aqueous fluid and frict ion reducing polymer. The sl urry fluid may comprise an aqueous fluid . The proppant ma\ comprise at least one particulate selected from the group consisting of silica sand, calci um carbonate sand, resin coated sand, ceramic, fly ash, and sintered bauxite. The proppant slurry may be pre-mixed be fore combini ng the carrier fl uid and the dispersing agent.

10020] In various examples, systems configured for deli vering the treatment fluids described herein to a dow nhole location are described. In various examples, the systems can comprise a pump tl uid ly coupled to a tubular, the tubular containing a treatment fluid comprisi ng a carrier fluid, proppant slurry, and optional additives. [002 1 ] The pump may be a high pressure pump in some examples. As used herein, the term "'high pressure pump" will refer to a pump that is capable of del ivering a fluid downhole at a pressure of about 1 000 psi or greater. A high pressure pump may be used when it is desired to introduce the treatment fl uid to a subterranean formation at or above a fracture gradient of the subterranean formation, but it may also be used in cases where fracturing is not desired. I n some examples, the high pressure pump may be capable of fl uidly conveying particulate matter, such as proppant, into the subterranean formation. Suitable high pressure pumps wi l l be known to one having ordinary skill in the art and may include, but are not l im ited to. floating piston pumps and positive displacement pumps.

[0022] In other examples, the pump may be a low pressure pump. As used herein, the term "low pressure pump" wil l refer to a pump that operates at a pressure of about 1000 psi or less. In some examples, a low pressure pump may be fluidly coupled to a high pressure pump that is fl uidly coupled to the tubular. That is, in such examples, the low pressure pump may be configured to convey the treatment fl uid to the high pressure pump. In such examples, the low pressure pump may "step up" the pressure of the treatment fluid before it reaches the high pressure pump.

[0023] In some examples, the systems described herein can further comprise a mixing tank that is upstream of the pump and in which the treatment fluid is formulated. In various examples, the pump {e.g. , a low pressure pump, a high pressure pump, or a combination thereof) may convey the treatment fl uid from the mixing tank or other source of the treatment fluid to the tubular. In other examples, however, the treatment fluid can be formulated offsite and transported to a worksite, in which case the treatment fluid may be introduced to the tubular via the pump directly from its shipping container (e.g., a truck, a railcar, a barge, or the l ike) or from a transport pi pel ine. In either case, the treatment fluid may be drawn into the pump, elevated to an appropriate pressure, and then introduced into the tubular for del ivery downhole

[0024] The FIGU R E shows an i l lustrative schematic of a system that can del iver fracturi ng fl uids to a dow nhole location, according to one or more examples. As described herein, the fracturing fl uids may comprise a carrier fluid, concentrated proppant sl urry, and optional additives. It should be noted that while the FIGURE general ly depicts a land-based system, it is to be recognized that l ike systems may be operated in subsea locations as wel l. As depicted i n the FIGURE, system 1 may i nclude mixing tank 10, in which a fracturing fl uid may be formulated. The fracturi ng fl uid may be conveyed via l ine 1 2 to wellhead 14, where the fracturi ng fl uid enters tubu lar 1 6, tubular 1 6 extendi ng from wel lhead 14 into subterranean formati on 1 8. Upon bei ng ej ected from tubular 1 6, the fracturing fl uid may subsequently penetrate into subterranean formation 1 8. Pump 20 may be configured to raise the pressure of the fracturing fl uid to a desired degree before its introduction into tubular 1 6. The fracturing fluid may be introduced into subterranean formation 1 8 at any stage of a fracturing operation. For example, the fracturing fluid may be introduced into the subterranean formation 1 8 after one or more factures have been initiated. Fractures may be i ntroduced for example by a pad stage. It is to be recognized that system 1 is merely exemplary in nature and various additional components may be present that have not necessarily been depicted in the FIGU RE in the interest of clarity. Non-l i miting additional components that may be present include, but are not limited to. supply hoppers, valves, condensers, adapters, joints, gauges, sensors, compressors, pressure control lers, pressure sensors, flow rate controllers, flow rate sensors, temperature sensors, and the l ike.

[0025] A lthough not depicted in the FIGURE, the fracturing fluid may, in some examples, flow back to wel l head 14 and exit subterranean formation 1 8. In some examples, the fracturing fl uid that has flowed back to wellhead 14 may subsequently be recovered and recirculated to subterranean formation 1 8.

[0026] It is also to be recognized that the disclosed treatment fl uids may also directly or indirectly affect the various downhole equipment and tools that may come into contact with the treatment fl uids during operation. Such equipment and tools may include, but are not l imited to, wel lbore casing, wellbore l iner, completion string, insert strings, drill string, coiled tubi ng, slickl ine. wirel ine, drill pipe, drill collars, mud motors, downhole motors and/or pumps, surface-mounted motors and/or pumps, centraiizers, turbol izers, scratchers, floats (e.g., shoes, col lars, valves, etc.), logging tools and related telemetry equipment, actuators (e.g.. electromechanical devices, hydromechanical devices, etc.), sliding sleeves, production sleeves, plugs, screens, fi lters, flow control devices (e.g., inflow control devices, autonomous i nflow control devi ces, outflow control devices, etc.), coupl ings (e.g. , electro-hydraulic wet connect, dry connect, i nd uctive coupler, etc. ). control l ines (e.g., electrical, fiber optic, hydraul ic, etc.). survei l lance l ines, dri ll bits and reamers, sensors or distributed sensors, downhole heat exchangers, valves and corresponding actuation devices, tool seals, packers, cement pl ugs, bridge plugs, and other wel lbore isolation devices, or components, and the l ike. Any of these components may be included in the systems generally described above and depicted in FIG U RE 1 .

[0027] At least a portion of the subterranean formation 1 8 may comprise a permeabi l ity rangi ng from a lower l i mit of about 0.1 nano Darcy (iiD). 1 nD. 1 0 nD. 25 nD. 50 n D. 1 00 nD. or 500 nD to an upper l i m it of about 1 0 m D. 1 niD. 500 microD. 1 00 microD. 1 0 microD. or 500 nD. and wherein the permeabi l ity may range from any lower limit to any upper limit and encompass any subset therebetween. Without limitation, the subterranean formation 1 20 may be considered an ultra-tight formation, for example, having a permeabi l ity of about 1 mD or less, which may be a shale formation, sandstone formation, or other type of rock formation.

[0028] For the sake of brevity, only certain ranges are expl icitly disclosed herein.

However, ranges from any lower limit may be combined with any upper limit to recite a range not expl icitly recited, as wel l as, ranges from any lower limit may be combined with any other lower l i mit to recite a range not explicitly recited, in the same way, ranges from any upper l imit may be combined with any other upper limit to recite a range not expl icitly recited. Additional ly, w henever a numerical range with a lower limit and an upper limit is disclosed, any number and any incl uded range fal ling within the range are specifical ly disclosed. In particular, every range of values (of the form, "from about a to about b," or, equivalently, "from approxi mately a to b," or, equivalently, "from approximately a-b") disclosed herei n is to be understood to set forth every number and range encompassed within the broader range of val ues even if not expl icitly recited. Thus, every point or individual value may serve as its own lower or upper limit combined with any other point or individual value or any other lower or upper limit, to recite a range not explicitly recited.

[0029] To facilitate a better understanding of the present disclosure, the fol lowing examples of certain aspects of some of the systems, methods and cement compositions are given. In no way should the fol lowing examples be read to limit, or define, the entire scope of the disclosure.

EXAMPLE 1

[0030] In thi s example, micro-proppant in the form of fly ash was analyzed for oxide composition. The results are displayed in Table 1 . The proppant has a mean particle size of approximately 5 microns.

K20 2.14% K 1 .78%

CaO 2.63% Ca 1 .88%

Ti02 1 .53% Ti 0.91 %

MnO 0.00% Mn 0.00%

Fe203 1 1 .62% Fe 8.1 3%

Sum 100.00% Sum 100.00%

Table 1 : Elemental Oxide Analysis of Proppant

[003 1 ] A concentrated proppant slurry was prepared by mixi ng 10 lb/gal micro- proppant, 10 GPT aminosi lane, and water. The concentrated proppant sl urry was then poured at approximately 45°, and it was observed that the concentrated proppant slurry flowed easily.

EXAMPLE 2

[0032] A second concentrated proppant slurry was prepared by mixing 1 0 lb/gal micro-proppant, 10 GPT of an ammonium salt copolymer acrylate, and water. The concentrated proppant slurry was then poured at approximately 45°, and it was observed that the concentrated proppant slurry flowed easily.

EXAMPLE 3

[0033] Two concentrated proppant slurries were prepared as in Example 1 . One concentrated proppant sl urry contained an aminosilane and the other did not. The concentrated proppant sl urries were then added at a concentration of 0.1 GPT to a sl ick water sol ution. The sl ick water was a mixture of friction reducer (FR) and water. It was observed that the individual particles of the proppant flocculated and sank to the bottom of the container in the sample without aminosilane. It was further observed that the concentrated proppant sl urry containing aminosi lane did not fall out of solution.

EXAMPLE 4

[0034] T wo concentrated proppant sl urries were prepared as in Example 2. One sl urry contained an ammoni um salt copolymer acrylate and the other did not. The concentrated proppant sl urries were then added at a concentration of 0.1 GPT to a sl ick water solution. The sl ick water was a mixture of friction reducer (FR) and water. It was observed that the individual particles of proppant flocculated and sank to the bottom of the container in the sample w ithout the ammoni um salt copolymer acrylate. It w as further observed that the proppant sampl e containing ammoni um salt copolymer acryl ate d id not fal l out of sol ution.