CN112225325A - Device and process for converting organic wastewater into fuel by using 28 microbial strains - Google Patents
Device and process for converting organic wastewater into fuel by using 28 microbial strains Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/101—Sulfur compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/12—Halogens or halogen-containing compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/34—Organic compounds containing oxygen
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/34—Organic compounds containing oxygen
- C02F2101/345—Phenols
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/36—Organic compounds containing halogen
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/38—Organic compounds containing nitrogen
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/40—Organic compounds containing sulfur
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Oil, Petroleum & Natural Gas (AREA)
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- Hydrology & Water Resources (AREA)
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- Environmental & Geological Engineering (AREA)
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Abstract
The invention relates to the field of organic wastewater treatment, in particular to a device and a process for converting organic wastewater into fuel by using 28 microbial strains, wherein the device collects and separately stores wastewater with different properties, detects the wastewater, reasonably allocates the wastewater according to the data of COD and BOD, allocates the allocated wastewater and self-made biological strains according to the ratio, and has the functions of deodorization, sterilization and solidification; under the conditions of normal temperature, normal pressure and anaerobic condition, carrying out fermentation acid production on the pretreated organic wastewater through 28 microbial strains; through multi-stage reaction, 28 kinds of microbial strains are injected to be effectively used as carriers of the accessories in the reaction tank, and the microbial strains are put once and used for the whole life. And (3) generating anabolism in the reaction fission, and converting the organic wastewater into a high-efficiency and clean microbial clean fuel liquid product under the action of 28 microbial strains.
Description
Technical Field
The invention relates to the field of organic wastewater treatment, in particular to a device and a process for converting organic wastewater into fuel by using 28 microbial strains.
Background
In the prior art, the technology of converting waste water into energy mainly utilizes organic waste water to produce methane and utilizes organic waste water to produce hydrogen.
The methane scientists in all countries in the world mix organic waste water with straws and organic rotten substances, and produce methane under the condition of microbial anaerobic fermentation with proper temperature, humidity and pH value, and the methane is widely used as a novel renewable energy source to replace petroleum and natural gas. But the investment return period of the methane prepared by fermenting the organic wastewater is about 5 years, and the economic added value is low. The method for producing hydrogen from organic wastewater by using a microbial fermentation method has the disadvantages of high manufacturing cost, difficult industrial development and difficult popularization and application. Therefore, there is a need for a device and a process capable of converting organic wastewater into fuel at a relatively high speed, which can solve the problem of organic wastewater treatment and develop new energy sources.
Disclosure of Invention
The invention aims to provide a device and a process for converting organic wastewater into fuel by using 28 microbial strains.
In order to achieve the purpose, the invention adopts the following technical scheme:
a process for converting organic wastewater into fuel using 28 microbial species is provided, comprising the steps of:
s1 wastewater pretreatment: collecting and separately storing waste water with different properties, detecting the waste water, reasonably blending the waste water according to the data of COD and BOD, and blending the blended waste water and self-made biological strains according to a ratio, wherein the biological strains have the functions of deodorization, disinfection and solidification;
s2 microbial fermentation: under the conditions of normal temperature, normal pressure and anaerobic condition, the pretreated organic wastewater is fermented by biological strains to produce acid, and then is sequentially introduced into six reaction tanks, wherein each reaction tank contains one or more microbial strains, all the reaction tanks contain 28 microbial strains, the pretreated wastewater is subjected to fission reaction to generate metabolism under the action of the 28 microbial strains, and the organic wastewater is converted into a semi-finished fuel to be stored in a semi-finished storage tank;
s3 refining of semi-finished fuel: filtering solid particles of the semi-finished fuel in a filtering mode, further purifying the semi-finished fuel in a high-temperature distillation mode, and distilling and liquefying to obtain the finished fuel.
Further, the biological strain is prepared by mixing a deodorant, an insecticide, a curing agent and biological alcohol, the deodorant comprises cut tobacco, saccharomycetes, anaerobic saccharomycetes, myceliophthora, sinking bacteria and nicotine bacteria, the insecticide comprises sterilization bacteria, saccharomycetes, anaerobic saccharomycetes, cut tobacco, sulfur powder and boluoqing, and the curing agent comprises vanillin.
Further, the volume ratio of the biological strains to the organic wastewater is 3: 10.
Further, the 28 kinds of microorganism strains comprise smelly acid cell bacteria, fire-extinguishing bacteria, sterilization bacteria, alcohol mother bacteria, anaerobic alcohol mother bacteria, biological bacteria, sinking bacteria, mushroom bacteria, wine bacteria, waterfall bacteria, actinomycetes, jellyfish bacteria, mold bacteria, vanillin bacteria, fire-assisting bacteria, nicotine bacteria, mycelial bacteria, tadpole bacteria, phosphate bacteria, carbon bacteria, smelly acid bacteria, sulfur bacteria, anaerobic bacteria, water membrane bacteria, carbon bacteria, pdey bacteria and floating bacteria.
Furthermore, the organic wastewater contains five substances of halogen and derivatives thereof, cones, oxygen-containing organic matters, nitrogen-containing compounds and sulfur-containing compounds, malodorous substances in the five substances are absorbed by cell membranes of microorganisms, so that the malodorous substances are degraded and converted into water-soluble substances which enter microbial cells, and the water-soluble substances are converted into organic acids in the reaction process in the microbial cells, and then the organic acids and the microbial bacteria are subjected to denaturation reaction to generate the microbial alcohol-based composite liquid fuel mainly containing alcohols.
The utility model provides a convert organic waste water into device of fuel with 28 kinds of microbial strains, includes that waste water mixes and filters biological fermentation tank, semi-manufactured goods storage tank, filter equipment, distillation plant and six retort bodies, every the retort body includes storage tank and retort, and storage tank and retort pass through the pipeline intercommunication, and the retort passes through the pipeline intercommunication with another storage tank, and six retort bodies communicate in proper order, waste water mixes and filters biological fermentation tank and the storage tank of the first retort body and passes through the pipeline intercommunication, and semi-manufactured goods storage tank communicates with the retort of the last retort body, and semi-manufactured goods storage tank communicates with filter equipment and distillation plant intercommunication in proper order with purification fuel.
Has the advantages that: the invention carries out pretreatment on the wastewater. Firstly, a wastewater collection pool with a certain scale and a plurality of matched wastewater pools and tanks designed according to daily output are built, and then a proper amount of biological agent is added to purify and deodorize wastewater; then the wastewater added with the microbial preparation is stirred, and the wastewater can be converted into a novel, efficient and petrochemical energy-replaceable microbial fuel by a multi-stage continuous reaction device automatic production line under the conditions of proper pH value, normal temperature, normal pressure and anaerobic condition by utilizing a microbial fermentation method and a biochemical reaction synthesis principle. The microbial fuel is a composite alcohol-based fuel, can replace coal, natural gas, liquefied gas, diesel oil and gasoline, and can be widely applied to hotels, restaurants, families and industrial boilers. The further purification can be applied to the fields of automobiles, agricultural implements, transport ships, hydrogen extraction, hydrogen energy filling and the like.
The invention has the advantages of innovative production process technology, low wastewater treatment cost, convenient industrial production, and good economic and social benefits, and solves the two problems of environmental pollution and energy scarcity. The method opens up a comprehensive utilization epoch for developing microorganism renewable energy sources.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings required to be used in the embodiments of the present invention will be briefly described below.
FIG. 1 is a process flow diagram of the present invention;
FIG. 2 is a diagram of an apparatus of the present invention;
FIG. 3 is a partial schematic view of an apparatus according to the present invention;
in the figure: 1, a mixing zone; 2, a microbial reaction zone; 3, a semi-finished product area; 4, a distillation zone; and 5, a finished product area.
Detailed Description
The technical scheme of the invention is further explained by the specific implementation mode in combination with the attached drawings.
Wherein the showings are for the purpose of illustration only and are shown by way of illustration only and not in actual form, and are not to be construed as limiting the present patent; to better illustrate the embodiments of the present invention, some components of the drawings may be omitted, enlarged or reduced, and do not represent the size of an actual product.
Example 1: referring to fig. 1, a process for converting organic wastewater into fuel using 28 microbial species includes the following steps:
s1 wastewater pretreatment: collecting and separately storing waste water with different properties, detecting the waste water, reasonably blending the waste water according to the data of COD and BOD, and blending the blended waste water and self-made biological strains according to a ratio, wherein the biological strains have the functions of deodorization, disinfection and solidification;
s2 microbial fermentation: under the conditions of normal temperature, normal pressure and anaerobic condition, the pretreated organic wastewater is fermented by biological strains to produce acid, and then is sequentially introduced into six reaction tanks, wherein each reaction tank contains one or more microbial strains, all the reaction tanks contain 28 microbial strains, the pretreated wastewater is subjected to fission reaction to generate metabolism under the action of the 28 microbial strains, and the organic wastewater is converted into a semi-finished fuel to be stored in a semi-finished storage tank;
s3 refining of semi-finished fuel: filtering solid particles of the semi-finished fuel in a filtering mode, further purifying the semi-finished fuel in a high-temperature distillation mode, and distilling and liquefying to obtain the finished fuel.
The biological strain is prepared by mixing a deodorant, a pesticide, a curing agent and biological alcohol, wherein the deodorant comprises tobacco shreds, saccharomycetes, anaerobic saccharomycetes, myceliophthora, sinking bacteria and nicotine bacteria, the pesticide comprises sterilization bacteria, saccharomycetes, anaerobic saccharomycetes, tobacco shreds, sulfur powder and purothuroblue, and the curing agent comprises vanillin.
The volume ratio of the biological strains to the organic wastewater is 3: 10.
The 28 microbial strains comprise smelly acid cell bacteria, fire-extinguishing bacteria, sterilization bacteria, alcohol mother bacteria, anaerobic alcohol mother bacteria, biological bacteria, sinking bacteria, mushroom bacteria, wine bacteria, waterfall bacteria, actinomycetes, jellyfish bacteria, mould, vanillin bacteria, fire-assisting bacteria, nicotine bacteria, myceliophthora, tadpole bacteria, phosphate bacteria, carbon bacteria, smelly acid bacteria, sulfur bacteria, anaerobic bacteria, water film bacteria, carbon bacteria, pdey bacteria and floating bacteria, and the floating bacteria can be one or more of floating bacteria.
The organic wastewater contains five substances of halogen and derivatives thereof, cones, oxygen-containing organic matters, nitrogen-containing compounds and sulfur-containing compounds, malodorous substances in the five substances are absorbed by cell membranes of microorganisms, so that the malodorous substances are degraded and converted into water-soluble substances which enter microbial cells, and the water-soluble substances are converted into organic acid in the reaction process in the microbial cells, and then the organic acid and the microbial bacteria are subjected to denaturation reaction to generate the microbial alcohol-based composite liquid fuel mainly containing alcohols.
Gases dissolved in high-concentration and malodorous organic wastewater are mixed according to the proportion of COD and BOD to be used as a product raw material, and the malodorous and volatile organic wastewater contains five types of substances:
(1) halogen and its derivatives: such as chlorine, halogenated cones, etc.;
(2) cones: such as alkane cones, alkene cones, skin cones, aromatic cones, etc.;
(3) oxygen-containing and organic matter: such as phenols, alcohols, aldehydes, ketones, fatty acids, and the like;
(4) a nitride-containing compound: ammonia, amines, tyramines, nitro-containing compounds;
(5) a sulfur-containing compound: such as hydrogen sulfide, thiols, sulfur, etc.;
the volatile malodorous substances are mostly organic compounds except hydrogen sulfide and ammonia. During the hydrolysis process of malodorous substances, microbial strains are added. The foul gas components dissolved in water are absorbed by the cell membrane of the microbial strains to generate corresponding enzymolysis to play a role, so that all the foul substances can be degraded and converted into water-soluble substances. These hydrolysates enter the microbial cells, participate in intracellular biochemical reactions and are converted to fatty acids during fermentation.
The working principle is as follows: firstly, pretreating organic wastewater, introducing the wastewater into a wastewater collection pool with a certain scale and a plurality of matched wastewater collection pools and tanks designed according to daily yield, introducing the wastewater into a wastewater blending pool from the wastewater collection pool, adding biological strains, blending the biological strains and the organic wastewater according to the actual condition of yield, and purifying and deodorizing the organic wastewater; the pretreated organic wastewater enters a wastewater biological fermentation tank and is matched with certain biological strains, the pretreated organic wastewater is stirred in the biological fermentation tank, and the microorganisms in the organic wastewater are fermented to produce acid under the conditions of normal temperature, normal pressure and anaerobic condition. After entering microbial cells, the hydrolysate is further decomposed into small molecular compounds under the action of intracellular enzymes, and the small molecular compounds are changed into a large amount of fatty acids, such as low-volatility fatty acids, alcohols, aldehydes, ketones, esters, carbon dioxide, carbohydrates (polysaccharides), free ammonia and the like, so that the pH value in the fermentation environment is reduced and the fermentation environment is acidic, and the fermentation acid production stage is called. In 6 reaction tanks, the organic wastewater is converted into composite liquid fuel under the action of microorganisms such as phosphate bacteria, carbon bacteria, fire-assisting bacteria and the like. At this stage, under the action of phosphoric acid bacteria, carbon bacteria, fire-supporting bacteria and biological agent, the microbial fermentation and biochemical reaction synthesis principle is used, the reaction tank body with multi-stage continuous reaction can produce a series of biochemical reactions of esterification, hydroxylation, oxidation and the like, the acid concentration of organic sewage is reduced, the original substance is denatured, the denatured molecules are recombined, and finally the composite liquid fuel is synthesized and then enters the product storage tank for packaging. The microbial clean fuel prepared by converting the organic wastewater by the process is a novel and efficient microbial liquid fuel capable of replacing petrochemical energy, and the organic components of the microbial clean fuel are CAS: 621-59-0, formula: C8H803, molecular weight: 152,15, boiling point: 179 ℃, melting point: 112 ℃ to 386 ℃.
The invention mainly comprises three stages, namely hydrolysis deodorization, fermentation acid production and biochemical alcohol production. The conversion synthesis mechanism of the biochemical alcohol production stage is divided into three stages of acid reaction, denaturation reaction and heating value reaction. According to Henry's law, the odor and pollutants of high-concentration foul sewage dissolved in water are decomposed and absorbed by microbial cells and secreted enzymes, and a large amount of fatty acids, mainly Volatile Fatty Acids (VFA) and alcohol, are generated in the decomposition process, so that the pH in the fermentation environment is reduced and is acidic. General organic odorants decompose carbon dioxide and water, sulfur-containing odorants decompose sulfurous acid and sulfuric acid, and nitrogen-containing odorants decompose nitrous acid and nitric acid. The microbial bacteria and various fatty acids are subjected to esterification reaction to generate formic acid, methyl ester and alcohols. Alcohol is oxidized into aldehyde by air, microbial strains and photospace generate hydroxylation reaction to generate methyl oxoformate, the methyl oxoformate further reacts to generate dimethyl carbonate, the dimethyl carbonate reacts with carbon monoxide and carbon dioxide to generate hydroxylation reaction to generate various products, and the alcohol-based composite fuel is mainly prepared from alcohol components, so the alcohol-based composite fuel is qualified as biological alcohol-based composite fuel. The microbial bacteria with the functions of catalysis, combustion supporting and stabilization are added into the last two biochemical reaction tanks, so that acid-containing organic matter molecules can be more active, the acidity is further reduced, the organic combustible substances are denatured, the carbon content is continuously increased, the product compatibility and stability are better, the combustion is more sufficient, the heat value is high, the use is safe and reliable, and no environmental pollution is caused. The fuel can replace coal, natural gas, liquefied gas, diesel oil and gasoline, and can be widely applied to hotels, guest houses, restaurants, families and industrial boilers. The further purification can be applied to the fields of automobiles, agricultural implements, transport ships, hydrogen extraction, hydrogen energy filling and the like.
Example 2: referring to fig. 2 and 3, an apparatus for converting organic wastewater into fuel using 28 microbial species is characterized in that: including waste water mixed filtration biological fermentation pond, semi-manufactured goods storage tank, filter equipment, distillation plant and six retort body, every the retort body includes storage tank and retort, and storage tank and retort pass through the pipeline intercommunication, and the retort passes through the pipeline intercommunication with another storage tank, and six retort body communicate in proper order, waste water mixed filtration biological fermentation pond passes through the pipeline intercommunication with the storage tank of the first retort body, and semi-manufactured goods storage tank and the retort intercommunication of the last retort body, semi-manufactured goods storage tank communicate with filter equipment and distillation plant in proper order with the purification, all adds the microorganism fungus class in the retort body and catches the carbon element in the air, constantly improves carbon element content in organic waste water in the conversion process. The filter is used for filtering sand, solid particles and other pollutants in the filter. The reaction tank is used for realizing the conversion of the organic wastewater into fuel and carrying out carbon capture.
The above disclosure is only for the purpose of illustrating the preferred embodiments of the present invention and should not be taken as limiting the scope of the present invention.
Claims (6)
1. A process for converting organic wastewater into fuel using 28 microbial species, comprising the steps of:
s1 wastewater pretreatment: collecting and separately storing waste water with different properties, detecting the waste water, reasonably blending the waste water according to the data of COD and BOD, and blending the blended waste water and self-made biological strains according to a ratio, wherein the biological strains have the functions of deodorization, disinfection and solidification;
s2 microbial fermentation: under the conditions of normal temperature, normal pressure and anaerobic condition, the pretreated organic wastewater is fermented by biological strains to produce acid, and then is sequentially introduced into six reaction tanks, wherein each reaction tank contains one or more microbial strains, all the reaction tanks contain 28 microbial strains, the pretreated wastewater is subjected to fission reaction to generate metabolism under the action of the 28 microbial strains, and the organic wastewater is converted into a semi-finished fuel to be stored in a semi-finished storage tank;
s3 refining of semi-finished fuel: filtering solid particles of the semi-finished fuel in a filtering mode, further purifying the semi-finished fuel in a high-temperature distillation mode, and distilling and liquefying to obtain the finished fuel.
2. The process for converting organic wastewater into fuel using 28 microbial species as claimed in claim 1, wherein: the biological strain is prepared by mixing a deodorant, a pesticide, a curing agent and biological alcohol, wherein the deodorant comprises tobacco shreds, saccharomycetes, anaerobic saccharomycetes, myceliophthora, sinking bacteria and nicotine bacteria, the pesticide comprises sterilization bacteria, saccharomycetes, anaerobic saccharomycetes, tobacco shreds, sulfur powder and purothuroblue, and the curing agent comprises vanillin.
3. The process for converting organic wastewater into fuel using 28 microbial species as claimed in claim 2, wherein: the volume ratio of the biological strains to the organic wastewater is 3: 10.
4. The process for converting organic wastewater into fuel using 28 microbial species as claimed in claim 3, wherein: the 28 kinds of microorganism strains comprise smelly acid cell bacteria, fire-extinguishing bacteria, sterilization bacteria, alcohol mother bacteria, anaerobic alcohol mother bacteria, biological bacteria, sinking bacteria, mushroom bacteria, wine bacteria, waterfall bacteria, actinomycetes, water mother bacteria, mold, vanillin bacteria, fire-boosting bacteria, nicotine bacteria, myceliophthora, tadpole bacteria, phosphate bacteria, carbon bacteria, smelly acid bacteria, sulfur bacteria, anaerobic bacteria, water film bacteria, carbon bacteria, pdey bacteria and floating bacteria.
5. The process for converting organic wastewater into fuel using 28 microbial species as claimed in claim 4, wherein: the organic wastewater contains five substances of halogen and derivatives thereof, cones, oxygen-containing organic matters, nitrogen-containing compounds and sulfur-containing compounds, malodorous substances in the five substances are absorbed by cell membranes of microorganisms, so that the malodorous substances are degraded and converted into water-soluble substances which enter microbial cells, and the water-soluble substances are converted into organic acid in the reaction process in the microbial cells, and then the organic acid and the microbial bacteria are subjected to denaturation reaction to generate the microbial alcohol-based composite liquid fuel mainly containing alcohols.
6. An apparatus for converting organic wastewater into fuel using 28 microbial species, comprising: including waste water mixed filtration biological fermentation pond, semi-manufactured goods storage tank, filter equipment, distillation plant and six retort bodies, every the retort body includes storage tank and retort, and storage tank and retort pass through the pipeline intercommunication, and the retort passes through the pipeline intercommunication with another storage tank, and six retort bodies communicate in proper order, waste water mixed filtration biological fermentation pond passes through the pipeline intercommunication with the storage tank of the first retort body, and semi-manufactured goods storage tank communicates with the retort of the last retort body, and semi-manufactured goods storage tank communicates with filter equipment and distillation plant in proper order with purification fuel.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| WO2010019935A2 (en) * | 2008-08-15 | 2010-02-18 | Brijen Biotech, Llc | Refinery process to produce biofuels and bioenergy products from home and municipal solid waste |
| CN102585924A (en) * | 2012-01-06 | 2012-07-18 | 深圳市海逖富生物科技股份有限公司 | Manufacturing process of compound liquid fuel |
| CN102911747A (en) * | 2012-11-22 | 2013-02-06 | 深圳市海逖富生物科技股份有限公司 | Production technology of composite liquid fuel |
| CN103910473A (en) * | 2014-04-18 | 2014-07-09 | 罗卫城 | Production process for converting organic sewage into liquid fuel |
| JP2015093940A (en) * | 2013-11-13 | 2015-05-18 | 水ｉｎｇ株式会社 | Method and device of producing liquid fuel |
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2020
- 2020-09-30 CN CN202011056841.6A patent/CN112225325A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2010019935A2 (en) * | 2008-08-15 | 2010-02-18 | Brijen Biotech, Llc | Refinery process to produce biofuels and bioenergy products from home and municipal solid waste |
| CN102585924A (en) * | 2012-01-06 | 2012-07-18 | 深圳市海逖富生物科技股份有限公司 | Manufacturing process of compound liquid fuel |
| CN102911747A (en) * | 2012-11-22 | 2013-02-06 | 深圳市海逖富生物科技股份有限公司 | Production technology of composite liquid fuel |
| JP2015093940A (en) * | 2013-11-13 | 2015-05-18 | 水ｉｎｇ株式会社 | Method and device of producing liquid fuel |
| CN103910473A (en) * | 2014-04-18 | 2014-07-09 | 罗卫城 | Production process for converting organic sewage into liquid fuel |
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Application publication date: 20210115 |