What I Claim:
1. I am claiming the method of proces$ing liquid organic waste, whereas sludge liquid is separated from sludge solid. The sludge solid is pasteurized and pumped into the formation Unit. The heat gases (heai, emission, air pressure, ash, dust, and etcetera) force sludge solid to move rnøre than 1 one direction creating ocean waves look alike and the liquid substance in sludge solid is! steamed out of the unit to designated location and the dried substance becomes an energy fuel product equivalent to coal.
2. (1 ) I am claiming the method of processing greenhouse gases, whereas cotton fiber is used to separate metals and solid from flu gases. The gases are injected into a purification agents or ^gent in the Purification Tank for neutralization and oxidized into water.
(I I) I am claiming the method of pfocess, whereas Sodium Peroxide/ lime, Sodium Peroxide/ Caustic Soda (NaOH), Sodium Peroxide/ Soda ASh (Na 2 CO 3 ), or ammonia (NH J ), and Sodium i Peroxide/ Limestone are used as purification agents or agent to neutralize greennoμse gases and convert the gases into solid or purified water.
(II I) I am claiming the method of pifocess to cool flu gases whereas the percolated gas output of the Gas Purification Tank is infused into a stream of coolant water which is recirculated from a Water Bath by a pump. The coolant water dissipates its heat by flowing down a staged water fall |
Patent Application Of Caiυs E. Egbufoama
Nigerian Citizen
5802 Annapolis Pd Apt 706
BladensbUrg, MdI 20710
For
Title of the Invention:
Method of Processing Liquid Organic Waste to Solid Fuel; Greenhouse Gas Purification and Oxidization:
Cross-Referertce to Related Applications
The present invention relates to complete improvement of two prior inventions- application number 10/630,902 and application number 11/215,75φ. The two prior inventions focused on condensation of municipal waste such as:- raw sewer, manure, milk emission, dust, ashes to solid, and renewable energy fuel product; the invention^ did not address the purification of the greenhouse gases before the gases are injected into tHe atmosphere. The current invention application number 11/518,702 provides a process to completely separate pathogen free organic fertilizer from renewable energy products and complete elimination of greenhouse gases such as Carbon Monoxide, Carbon Dioxide, Sulphur Dioxin, Lead, Mercury, Hydrocarbon,, Hydrogen Sulfide, ammonia, Nitrogen, and all other gase? from entering into the atmosphere. In the latest invention greenhouse gases are purified and released as, liquid into the environment.
Invention Background
My name is Caius Emeka Egbufoama and I ajm a native of Nigeria. I hold a degree in Electrical
Engineering. I am currently working on my se«tx>nd degree in Chemistry from Federal University of
Technology Imo-State Nigeria. I am Currently operating my pilot plant in Nigeria and working on new technology that will better preserved the environment.
I am also aware of the current technology sip as Scrubber to lower the emission stack. I was drawn into this invention by my interest in cieaφ environment, global worming, health concerns, and alternative energy source.
Summary:
The technology process converts liquid organic! waste such as:- raw sewer, raw manure, and etcetera to solid energy producing products; wtjereas the greenhouse gas is processed by separating solid, metals from the flu gases. Th^ flu gases from greenhouse gases (combination various gas agents) are purified with vaiious cleaning agents or agent and oxidized to a single gas. The gas is converted into liquid that is θnvironnfiental friendly and released at a room temperature depending on the atmospheric temperature. Tlfie solid and metals extracted from greenhouse gas are treated and released as an aggregated products.
Procedure:
Method of Processing Liquid Organic Waste tolSolid Fuel; Greenhouse Gas Purification and
Oxidization to purified water:
Component Identification: for Figure 1
1. Combustion Unit
2. Heat Control and Distribution
3. intake Buffer
4. Formation Processor Tank
5. Drain (Cycle 1)
6. Drying Processor Tank
7. Drain (Cycle 2)
8. Distillate Outputs
9. Lock Controls for Distillate Piping
10. Staged Sedimentation Column
11. Stage 1 Sedimentation
12. Stage 2 Sedimentation
13. Stage 3 Sedimentation
14. Stage 4 Final Cooling
15. Vapor Output
16. Combustible Fuel Output
17. Sedimented Organic Output
18. Reduced Fuel (Ash) Output Process Annotation:
A) Inputs consist of:
• Agricultural-Inputs, Following standard, septic sedimentation
• CIVIL-lnputs, Following TBD waste treatment specs
B) Combustion Unit provides controlled high-jtemperature injection for both Formation and Drying processes.
C) Inputs are loaded into Formation lank, where most of the organics are distilled away. Heat injectors provide agitation to the base of thø materials. Cycle 1 is performed when moisture content drops to specified threshold.
D) Drying process drives out remaining moisture to specified threshold. Cycle 2 drains reduced materials.
E) High-temperature distillates are cooled in| stages where organic particulates are sedimented. Tanks are sealed, so distillate pressures forc^ vapors up through each tank. When lowest tank is saturated, its organics are drained, and each htørier tank is sequentially drained into the lower tank, and fresh (or condensed) water is added to the, iop tank. To keep production constant, the use 2 or more complete columns will allow drainage anijj service while one column remains in operation.
To purify the fluid gas from the water vapor out-put 15 (shown on figure 1 drawing), the flu gas is collected in central collector (1), (shown on figure 2) before being fed into one of several parallel expansion chambers (2) which serve to lower the initial gas temperature by increasing the overall volume of the output stack.
Gases and particulates pass through a shroud (3) which collects particulates for removal during cleaning by a side cieanout port (4). Moistened fiber filters (5) surround vent tubes (6), which remove the majority of the first-stage particulu^s. These filters must be changed or cleaned in a regularly calculated cycle.
Gases leaving this stage are collected in Manifolds (7) which join the outputs of all parallel expansion chambers prior to feeding into a blower unit (8) which maintains negative pressure in all the output manifolds and feeds the combined IPhase 1" outputs into the secondary collector (9). The scrubbing process is repeated again in lits entirety through the secondary scrubber system (10).
The output gases (Sulfur Dioxin, CO 1 COz , ptc.) of the secondary scrubber (11) are percolated through a Gas Purification tank (12) Sodium Peroxide/ lime are mechanical injected (sprayed) into the Gas Purification tank such that the reagent droplets absorb the flu gas {greenhouse gas) while simultaneously being dried. There are basic principles to obtain maximum reactor and maximum purification of flu gas: (a) the length and sizel of the Gas Purification tank, (b) The flow (Pressure level) and the flow direction of greenhouse jjas injecting into the Gas Purification tank, (c) The positioning of the Sodium Peroxide/ lime spryior inject valve into the Gas Purification tank, (d) the positioning and the size of the flu gas outlet ivalve from the Gas Purification tank to designated location.
To obtain one hundred percent (100%) puritiφatton of greenhouse gas, the greenhouse injection valve from the Filter tank into the Gas Purification tank has to be inches above the bottom of the Gas Purification tank so that when greenhouse gas is injected into the vessel it will travel to the bottom of the vessel first and then travel up. As the greenhouse gas travels up in the vessel {Gas Purification tank) it mixes with Sodium Peroxide/ lime injecting into the vessel and the greenhouse gas is absorbed by Sodium Peroxide/ lime and tie chemical reaction is taking place. In other to obtain one hundred percent (100tø>) chemical reaction and purification" (a) the gas entering and exiting the Gas Purification tan|κ must flow in one direction, (b) gas in the Gas Purification tank has to travel from the bottom of the vessel to the top of the vessel within five (5) seconds or above and no less, (c) the Flu Gas outlet valve has to be positioned in the middle of the
vessel and the size of the valve has to be considered to two main reasons: (1) to hold greenhouse gas in the Gas Purification tank for a minimum oi thirty (30) seconds and above reaching 100% completion, and (2) safety reasons (avoid setting of bomb). The theories for obtaining one hundred percent (100%) greenhouse gas purification are: (1) separate the solid, metals, and flareable substances from flu gas, (2) the taller or longeή the purification vessel the better completion.
The percolated gas output of the Gas Purification tank (13) is infused into a stream of coolant water
(14) which is recirculated from a Water Bath { " |5) by a Pump (16). The coolant water dissipates its heat by flowing down a staged waterfall (1|7). Furthermore, the process and purification of greenhouse gases can be implemented at sta^e 1 sedimentation.
Lab experiment:
Reagent determined and the overall material balances (in Kg) are shown below:-
Reagent slurry mixture CaO=O.053,
CO 2 =0.143, CO=0.023, SO 2 =0.061, N 2 =0.714, O 2 =0.012 injected into the reactor. The exit flu gas N 2 =0.714, 01 =0.012, CO 2 =0.014, H 2 OF=0,230; non toxic disposable sludge CaSO 4 =0.540, and Na 2 CO 3 =0.432