CN105861283A - Miniature methane-producing devices - Google Patents
Miniature methane-producing devices Download PDFInfo
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- CN105861283A CN105861283A CN201610289152.7A CN201610289152A CN105861283A CN 105861283 A CN105861283 A CN 105861283A CN 201610289152 A CN201610289152 A CN 201610289152A CN 105861283 A CN105861283 A CN 105861283A
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- methane
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- phase device
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M43/00—Combinations of bioreactors or fermenters with other apparatus
- C12M43/04—Bioreactors or fermenters combined with combustion devices or plants, e.g. for carbon dioxide removal
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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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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
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- Organic Chemistry (AREA)
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- Bioinformatics & Cheminformatics (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- General Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
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- General Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Sustainable Development (AREA)
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- Molecular Biology (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Provided are miniature methane-producing devices. A methane-producing device (10) is internally provided with multiple miniature methane-producing devices (11), each miniature methane-producing device comprises a concave cover (1), a water electrolysis device (2) and a coal-oil-gas waste gas output pipe orifice (3), and the miniature methane-producing devices are characterized in that methane bacteria are put in the methane-producing device (10), a nutrient solution is injected, waste gas which is exhausted when coal-oil-gas equipment (13) works is conveyed to a gas distributor (12) in the methane-producing device (10) through a pipeline, the gas distributor (12) distributes the waste gas to all the miniature methane-producing devices (11), the waste gas is output from the waste gas output pipe orifice (3), carbon dioxide in the waste gas rises and meets with hydrogen ions produced by the water electrolysis device (2), and methane is synthesized under the action of the methane bacteria; meanwhile, oxygen, hydrogen and carbon dioxide are produced and called by a joint name of methane gas mixture which is output as soon as producing, harm of oxygen to the methane bacteria is reduced to the minimum extent, the situation of preparing methane from the coal-oil-gas waste gas becomes possible from impossible, and energy self sufficiency, zero-emission exhaust and zero pollution of the coal-oil-gas equipment are achieved.
Description
Technical field
The present invention relates to a kind of coal and oil combustion gas waste gas and produce the device of methane, a kind of miniature methane phase device.
Background technology
Currently, to produce methane the most blank for coal and oil combustion gas waste gas.Therefore, methane device is produced in a kind of coal and oil combustion gas of design, is to be badly in need of at present solving the technical problem that.
Summary of the invention
The technical problem to be solved is to provide a kind of coal and oil combustion gas waste gas and produces the device of methane.
The present invention solves the technical scheme of its technical problem:
Miniature methane phase device, in methane phase device, multiple miniature methane phase device is set, methane backeria kind is filled in methane phase device, fill nutritional solution, the waste gas that coal and oil gas-fired equipment operationally discharges, waste gas is pipelined to the gas diverter in methane phase device, waste gas is diverted to each miniature methane phase device by gas diverter, export from exhaust output tube mouth, carbon dioxide in waste gas rises, the hydrion produced with water electrolysis equipment meets, synthesizing methane under the effect of methane backeria, simultaneously, also produce oxygen, hydrogen and carbon dioxide, it is referred to as methane mixed gas, when methane mixed gas methane rate is more than 50%, methane mixed gas is delivered directly to combustion apparatus burning, the waste gas discharged again, it is transported to miniature methane phase device again, export from exhaust output tube mouth.Methane mixed gas methane rate is less than 50%, methane mixed gas is transported to methane purifier, methane purifier is by methane, carbon dioxide, oxygen, Hydrogen Separation, methane oxygen hydrogen is transported to combustion apparatus burning, the waste gas discharged again, it is transported to miniature methane phase device again, export from exhaust output tube mouth, isolated carbon dioxide is delivered directly to miniature methane phase device, export from exhaust output tube mouth, it is achieved coal and oil gas-fired equipment waste gas circulation utilizes, power self-support, zero waste gas emission, no pollution.
As a kind of priority scheme of the present invention, miniature methane phase device, including spill cover and water electrolysis equipment and coal and oil combustion gas exhaust output tube mouth.It is provided with methane mixed gas outlet tube on the top of miniature methane phase device, spill cover is made up of top plate and lower plywood, top plate lower end is right angle, lower end, right angle is apron, lower plywood top is provided with methane mixed gas rise hole, methane mixed gas outlet tube is provided with water electrolyzer below, and water electrolyzer is provided with coal and oil combustion gas exhaust output tube mouth below.The coal and oil combustion gas waste gas of gas transmission mouth of pipe output rises the hydrion operationally produced with water electrolysis equipment and meets, under the effect of methane backeria, and synthesizing methane, but the most also produce the gases such as oxygen, hydrogen and carbon dioxide, it is referred to as: methane mixed gas.But oxygen can make methane backeria dead.And miniature methane phase device can make, with the methane mixed gas produced, with rising, by the hole on spill cover top, to rise to methane mixed gas outlet tube and export.Meanwhile, the mud that methane mixed gas carries when rising sinks to the following right angle of spill cover to the interlayer of spill cover, enters in methane phase device.
Operation principle: coal and oil combustion gas waste gas is pipelined to the gas diverter in methane phase device, waste gas is diverted to each miniature methane phase device by gas diverter, carbon dioxide in coal and oil combustion gas waste gas rises the hydrion produced with water electrolysis and meets, under the effect of methane backeria, synthesizing methane.In this course, also produce oxygen, hydrogen, also have the gases such as carbon dioxide, be referred to as: methane mixed gas.Wherein, oxygen can make methane backeria dead.In order to prevent methane backeria dead, multiple miniature methane phase device is set in methane phase device, miniature methane phase device can make methane mixed gas with generation, with output.Make the oxygen hazardness to methane backeria, be reduced to minimum, make coal and oil combustion gas waste gas produce methane by not becoming possibility.
Compared with prior art, coal and oil combustion gas waste gas is made to produce methane by not becoming possibility.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Fig. 2 is the structural representation of miniature methane phase device.
Detailed description of the invention
nullAs shown in the figure,Miniature methane phase device,In methane phase device 10,Multiple miniature methane phase device 11 is set,At methane phase device 10 built-in methane strain,Note nutritional solution,The waste gas that coal and oil gas-fired equipment 13 operationally discharges,Waste gas is pipelined to the gas diverter 12 in methane phase device 10,Waste gas is diverted to each miniature methane phase device 11 by gas diverter 12,Export from exhaust output tube mouth 3,Carbon dioxide in waste gas rises,The hydrion produced with water electrolyzer 2 meets,Synthesizing methane under the effect of methane backeria,Simultaneously,Also produce oxygen、Hydrogen and carbon dioxide,It is referred to as methane mixed gas,When methane mixed gas methane rate is more than 50%,Methane mixed gas is delivered directly to combustion apparatus 13 and burns,The waste gas discharged again,It is transported to miniature methane phase device 11 again,Export from exhaust output tube mouth 3,Methane mixed gas methane rate is less than 50%,Methane mixed gas is transported to methane purifier 14,Methane purifier 14 is by methane、Carbon dioxide、Oxygen、Hydrogen Separation,Methane oxygen hydrogen is transported to combustion apparatus 13 and burns,The waste gas discharged again,It is transported to miniature methane phase device 11 again,Export from exhaust output tube mouth 3,Isolated carbon dioxide is delivered directly to miniature methane phase device 11,Export from exhaust output tube mouth 3.
Miniature methane phase device, including spill cover 1 and water electrolyzer 2 and coal and oil combustion gas exhaust output tube mouth 3, it is characterized in that, spill cover 1 top is provided with methane mixed gas outlet tube 4, and spill cover 1 is made up of top plate 6 and lower plywood 7, and top plate 6 lower end is right angle 8, lower end, right angle is apron 5, lower plywood 7 top is provided with methane mixed gas rise hole 9, and methane mixed gas outlet tube 4 is provided with water electrolyzer 2 below, and water electrolyzer is provided with coal and oil combustion gas exhaust output tube mouth 3 below.
Claims (2)
- The most miniature methane phase device, in methane phase device (10), arranges multiple miniature product Methane device (11), it is characterised in that at methane phase device (10) built-in methane strain, Note nutritional solution, the waste gas that coal and oil gas-fired equipment (13) operationally discharges, waste gas passes through Pipeline is transported to the gas diverter (12) in methane phase device (10), gas diverter (12) Waste gas is diverted to each miniature methane phase device (11), exports from exhaust output tube mouth (3), Carbon dioxide in waste gas rises, and the hydrion produced with water electrolysis equipment (2) meets, at methane Synthesizing methane under the effect of bacterium, meanwhile, also produces oxygen, hydrogen and carbon dioxide, system Being referred to as methane mixed gas, when methane mixed gas methane rate is more than 50%, methane mixed gas is direct It is transported to combustion apparatus (13) burning, then the waste gas discharged, then is transported to miniature methane phase dress Putting (11), export from exhaust output tube mouth (3), methane mixed gas methane rate is less than 50%, Methane mixed gas is transported to methane purifier (14), methane purifier (14) by methane, two Carbonoxide, oxygen, Hydrogen Separation, methane oxygen hydrogen is transported to combustion apparatus (13) burning, The waste gas discharged again, then it is transported to miniature methane phase device (11), from exhaust output tube mouth (3) Output, isolated carbon dioxide is delivered directly to miniature methane phase device (11), from waste gas The output mouth of pipe (3) output, it is achieved coal and oil gas-fired equipment power self-support, zero waste gas emission, No pollution.
- Miniature methane phase device the most according to claim 1, miniature methane phase device bag Include spill cover (1) and water electrolysis equipment (2) and coal and oil combustion gas exhaust output tube mouth (3), It is characterized in that, spill cover (1) top is provided with methane mixed gas outlet tube (4), spill cover (1) Being made up of top plate (6) and lower plywood (7), top plate (6) lower end is right angle (8), right angle Lower end is apron (5), and lower plywood (7) top is provided with methane mixed gas rise hole (9), first Methane mixed gas outlet tube (4) is provided with water electrolyzer (2) below, and water electrolyzer is provided with below Coal and oil combustion gas exhaust output tube mouth (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201610289152.7A CN105861283A (en) | 2016-04-25 | 2016-04-25 | Miniature methane-producing devices |
Applications Claiming Priority (1)
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CN201610289152.7A CN105861283A (en) | 2016-04-25 | 2016-04-25 | Miniature methane-producing devices |
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CN105861283A true CN105861283A (en) | 2016-08-17 |
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CN201610289152.7A Pending CN105861283A (en) | 2016-04-25 | 2016-04-25 | Miniature methane-producing devices |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108753845A (en) * | 2018-07-19 | 2018-11-06 | 高节义 | The method of carbon dioxide preparation methane and its setting |
CN109554282A (en) * | 2018-03-01 | 2019-04-02 | 高节义 | Setting of the oxygenerator in conjunction with methane phase equipment |
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CN2615127Y (en) * | 2003-05-16 | 2004-05-12 | 天津大学 | Upflow type composite bed biological reactor with regulating three-phase separator |
CN101628754A (en) * | 2009-08-13 | 2010-01-20 | 浙江大学 | Two-phase integrated anaerobic digestion reaction vessel |
CN101691256A (en) * | 2009-09-08 | 2010-04-07 | 南开大学 | Tri-phase separator of anaerobic reactor |
CN101955294A (en) * | 2009-12-01 | 2011-01-26 | 南京大学 | Integrated bioreactor as well as application thereof and method for treating high-concentration organic wastewater |
CN202279690U (en) * | 2011-10-31 | 2012-06-20 | 庞玉学 | Combustion nozzle and secondary reforming furnace |
CN102874994A (en) * | 2012-10-30 | 2013-01-16 | 山东大学 | Double-internal circulating water treatment device capable of combining photocatalysis and aerobe, and working method thereof |
CN203754712U (en) * | 2014-01-23 | 2014-08-06 | 浙江大学 | Integrated dry-process anaerobic fermentation device for organic household garbage |
CN204281408U (en) * | 2014-12-11 | 2015-04-22 | 郭玉芳 | A kind of town water purification reactor |
CN204529850U (en) * | 2015-03-26 | 2015-08-05 | 高节义 | Coal combustion exhaust produces the device of methane |
CN204981513U (en) * | 2015-08-29 | 2016-01-20 | 中山市中开环保设备制造有限公司 | Treatment unit for pesticide -containing wastewater |
CN105463048A (en) * | 2015-03-26 | 2016-04-06 | 高节义 | Method for preparing methane from coal combustion exhaust and device thereof |
CN105483162A (en) * | 2015-12-10 | 2016-04-13 | 高节义 | Device of method for methane production and sulfur removal through coal, oil and gas exhaust gas and electrolysis |
CN205874392U (en) * | 2016-04-25 | 2017-01-11 | 高节义 | Miniature product methane device |
-
2016
- 2016-04-25 CN CN201610289152.7A patent/CN105861283A/en active Pending
Patent Citations (14)
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CN1421401A (en) * | 2002-12-30 | 2003-06-04 | 四川大学 | Biological treating equipment suitable for organic waste water |
CN2615127Y (en) * | 2003-05-16 | 2004-05-12 | 天津大学 | Upflow type composite bed biological reactor with regulating three-phase separator |
CN101628754A (en) * | 2009-08-13 | 2010-01-20 | 浙江大学 | Two-phase integrated anaerobic digestion reaction vessel |
CN101691256A (en) * | 2009-09-08 | 2010-04-07 | 南开大学 | Tri-phase separator of anaerobic reactor |
CN101955294A (en) * | 2009-12-01 | 2011-01-26 | 南京大学 | Integrated bioreactor as well as application thereof and method for treating high-concentration organic wastewater |
CN202279690U (en) * | 2011-10-31 | 2012-06-20 | 庞玉学 | Combustion nozzle and secondary reforming furnace |
CN102874994A (en) * | 2012-10-30 | 2013-01-16 | 山东大学 | Double-internal circulating water treatment device capable of combining photocatalysis and aerobe, and working method thereof |
CN203754712U (en) * | 2014-01-23 | 2014-08-06 | 浙江大学 | Integrated dry-process anaerobic fermentation device for organic household garbage |
CN204281408U (en) * | 2014-12-11 | 2015-04-22 | 郭玉芳 | A kind of town water purification reactor |
CN204529850U (en) * | 2015-03-26 | 2015-08-05 | 高节义 | Coal combustion exhaust produces the device of methane |
CN105463048A (en) * | 2015-03-26 | 2016-04-06 | 高节义 | Method for preparing methane from coal combustion exhaust and device thereof |
CN204981513U (en) * | 2015-08-29 | 2016-01-20 | 中山市中开环保设备制造有限公司 | Treatment unit for pesticide -containing wastewater |
CN105483162A (en) * | 2015-12-10 | 2016-04-13 | 高节义 | Device of method for methane production and sulfur removal through coal, oil and gas exhaust gas and electrolysis |
CN205874392U (en) * | 2016-04-25 | 2017-01-11 | 高节义 | Miniature product methane device |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109554282A (en) * | 2018-03-01 | 2019-04-02 | 高节义 | Setting of the oxygenerator in conjunction with methane phase equipment |
CN108753845A (en) * | 2018-07-19 | 2018-11-06 | 高节义 | The method of carbon dioxide preparation methane and its setting |
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