CN108315233A - Air produces the device of methane - Google Patents
Air produces the device of methane Download PDFInfo
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- CN108315233A CN108315233A CN201810185284.4A CN201810185284A CN108315233A CN 108315233 A CN108315233 A CN 108315233A CN 201810185284 A CN201810185284 A CN 201810185284A CN 108315233 A CN108315233 A CN 108315233A
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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
- C12M43/00—Combinations of bioreactors or fermenters with other apparatus
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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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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/70—Assemblies comprising two or more cells
- C25B9/73—Assemblies comprising two or more cells of the filter-press type
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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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- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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- Oil, Petroleum & Natural Gas (AREA)
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Abstract
Air produces the device of methane,It is made of with energy equipment (3) air oxygenerator (1) and methane phase equipment (2) and life,It is characterized in that,The carbon dioxide gas outlet (4) of air oxygenerator (1) is connected to by pipeline with the air inlet (6) of the diffluence room (5) of methane phase equipment (2),Carbon dioxide gas is out of, diffluence room (5) enters methane phase equipment (2) methane phase room (7),Continue to rise,Carbon dioxide is in methane phase room (7) uphill process,Generate methane,Methane continues to rise in methane phase room (7),Into the separation chamber (8) of methane phase equipment (2),Methane is discharged from the gas discharge outlet (9) of separation chamber (8),Gas discharge outlet (9) is connected to by pipeline with life with energy equipment (3),Methane mixed gas burns (acting) in life energy equipment (3),Discharge exhaust gas.
Description
Technical field
The present invention relates to the devices that a kind of air produces methane.
Background technology
Currently, China and world's air produce the device technique or blank of methane.
Invention content
The technical problem to be solved by the present invention is to：Air produces the device technique scheme of methane.
The present invention the technical solution to solve the technical problem is that：
Air produces the device of methane, is made of with energy equipment air oxygenerator and methane phase equipment and life.Air system
The oxygen that oxygen machine is produced is sold to user as commodity.The carbon dioxide gas that air oxygenerator is produced is logical from outlet
Piping is transported to the diffluence room of methane phase equipment.Carbon dioxide gas enters the methane phase room of methane phase equipment from diffluence room
It is interior, continue to rise.Carbon dioxide generates methane in the uphill process of methane phase room.Gas componant has methane, titanium dioxide at this time
Carbon, hydrogen, oxygen and other gases, are referred to as：Methane mixed gas, methane mixed gas continue to rise in methane phase room, enter
The separation chamber of methane phase equipment, methane mixed gas are discharged from the gas discharge outlet of separation chamber, and gas discharge outlet passes through pipeline
To life energy equipment, methane mixed gas is used in life to burn (acting) in equipment, discharge exhaust gas.It can also be in cathode chamber
Topmost cathode plate is not boxed out, and prevents hydrogen from entering methane phase room, and in cathode chamber topmost to being externally provided with hydrogen gas outlet.Hydrogen
After gas output, store, hydrogen is as merchandise sales.
As a preferred embodiment of the present invention, further includes liquefaction pond, fill up organic matter in liquefaction pond first, fill
Water makes organic matter be dissolved into water, forms organic water, this process is named liquefaction.The organic water outlet in liquefaction pond passes through pipeline
It is respectively delivered to being connected into liquid port for recovery centre of methane backeria poisoning treatment 12 and recovery centre of methane backeria poisoning treatment 13, first
The sludge water of recovery centre of Wan Jun poisoning treatments 12 and recovery centre of methane backeria poisoning treatment 13 is discharged from outlet, and sludge water is logical
Piping is transported to diffluence room, and sludge water namely for methane strain enters methane phase room from diffluence room, continues to rise, into separation chamber,
Sludge water from the outlet of the sludge water of separation chamber be discharged, outlet by pipeline respectively with recovery centre of methane backeria poisoning treatment
12 are connected to recovery centre of methane backeria poisoning treatment 13 into the sludge mouth of a river (15), and sludge water namely for methane strain recycles.First
In recovery centre of Wan Jun poisoning treatments (12) and recovery centre of methane backeria poisoning treatment 13, because the proportion of sludge is more than 1, under sludge
It is heavy, in bottom；Top is supernatant.Recovery centre of methane backeria poisoning treatment 12 and recovery centre of methane backeria poisoning treatment 13 it is upper
Portion is respectively equipped with liquid outlet, and liquid outlet be connected to liquefaction pond into liquid port respectively by pipeline, and liquid circulation is sharp
Use zero-emission.The top of recovery centre of methane backeria poisoning treatment 12 and recovery centre of methane backeria poisoning treatment 13 is additionally provided with natural pond respectively
Gas outlet, biogas outlet are connected to by pipeline with life with energy equipment.Recovery centre of methane backeria poisoning treatment 12 and methane
The effect of recovery centre of bacterium poisoning treatment 13：It first will be in recovery centre of sludge water namely for methane strain injection methane backeria poisoning treatment；
Also in methane phase room, when the hydrogen ion that carbon dioxide and water electrolysis generate, synthesizing methane under the action of methane backeria, together
When, discharge oxygen；Second is that the oxonium ion that cathode plate generates.Oxygen and oxonium ion can inhibit methane backeria movable, or even make methane
Bacterium is dead.Aerobic bacteria in recovery centre of methane backeria poisoning treatment 12 eats up the oxygen of methane backeria carrying, makes methane backeria rehabilitation.When
When the quantity of methane backeria death is more than the quantity of breeding, recovery centre of methane backeria poisoning treatment 12 is at this moment closed.Start methane backeria
Recovery centre of poisoning treatment 13, from recovery centre of methane backeria poisoning treatment 13 extract sludge water inject diffluence room, sludge water from point
Flow chamber enters methane phase room, and sludge water enters separation chamber from methane phase ceiling portion, is discharged from outlet, automatic back flow to methane backeria
Recovery centre of poisoning treatment 13, sludge water circulation use zero-emission.At this point, extracting organic water injection methane backeria poisoning from liquefaction pond
Therapy rehabilitation center 12, organic water rise in recovery centre of methane backeria poisoning treatment 12, are discharged from top outlet, overflow
To liquefaction pond, organic water circulation use zero-emission.In this course, methane backeria obtains breeding growth body key.Methane backeria is poisoned
Therapy rehabilitation center 12 and recovery centre of methane backeria poisoning treatment 13, which exchange, to be used.But recovery centre of methane backeria poisoning treatment 12
With recovery centre of methane backeria poisoning treatment 13, when working at the same time, working performance is different.
Further include that methane phase equipment is equipped with methane phase room, cathode chamber, anode chamber as a preferred embodiment of the present invention,
Gap between anode plate and cathode plate is methane phase room, and the gap between cathode plate and cathode plate is cathode chamber, anode plate with
Gap between anode plate is anode chamber.Cathode plate, anode plate are respectively equipped with hole.Anode plate, cathode plate outside be equipped with electrolysis
Diaphragm.Anode chamber, cathode chamber, methane phase room are referred to as：It is electrolysed three Room.Under the shell top of diffluence room and the shell of separation chamber
Side is respectively equipped with trouser legs, in the trouser legs for the top that the shell for being electrolysed three Room is inserted in diffluence room below.It is electrolysed the upper of the shell of three Room
While being inserted in the following trouser legs in separation chamber, three Room of electrolysis, diffluence room, separation chamber is made to be fixed together, forms methane phase equipment.
Operation principle：The carbon dioxide of oxygenerator production, by air pump, the diffluence room of pipeline to methane phase equipment,
Carbon dioxide enters from diffluence room in methane phase room, rapid to rise.At this point, water electrolyzer is started to work, anode chamber and cathode chamber
Hydraulic pressure is more than the hydraulic pressure of methane phase room, makes the water in cathode chamber and anode chamber under the action of hydraulic pressure, flows to methane phase room automatically.
The hydrogen ion that anode plate generates forms hydrogen ion water, first, the hydraulic pressure of the hydrogen ion water of anode chamber is more than methane phase in anode chamber
The pressure of the sludge water of room, hydrogen ion water flow to methane phase room automatically under the action of hydraulic pressure, by asymmetric diaphragm.Second is that hydrogen
Ionized water is under cathode plate attraction, by asymmetric electrolyte membrane into cathode plate transfer process, when passing by methane phase room.Hydrogen from
Hydrogen ion in sub- water meets in methane phase room and carbon dioxide and the methane backeria in sludge water, and carbon dioxide and hydrogen ion are in first
Under the action of alkane bacterium, synthesizing methane.Meanwhile also discharging oxygen.Methane gas and oxygen rise, and enter from methane phase ceiling portion and divide
From room, it is discharged from the gas discharge outlet of separation chamber；The hydrogen ion slipped through the net enters cathode chamber, and hydrogen ion is combined with hydrogen ion, generates
Hydrogen, hydrogen rise, the hole through cathode plate and electrolyte membrane from cathode chamber topmost, into methane phase room, from methane phase room
Top enters separation chamber, is discharged from the gas discharge outlet of separation chamber；The oxonium ion that cathode plate generates is shifted to anode plate, in anode
Room oxonium ion is combined with oxonium ion generation oxygen, and oxygen rises, the hole through anode plate and electrolyte membrane from anode chamber's topmost,
Into methane phase room, enter separation chamber from methane phase ceiling portion, is discharged from the gas discharge outlet of separation chamber.Gas from separation chamber
The gas of outlet discharge has：The gases such as methane, oxygen, hydrogen, carbon dioxide, are referred to as：Methane mixed gas.Methane mixed gas
Being pipelined to life can equipment, burning (acting), discharge carbon dioxide and water.Life energy equipment：Cooking stove,
Boiler, water heater, family heating system etc..Life energy equipment can be realized：Zero consumption conventional energy resource, zero oxygen consumption gas, zero
Pollution.During being electrolysed three Room and producing methane, the oxygen of release and the oxygen of generation and carbon dioxide conversion be methane with
At work with energy equipment, the carbon dioxide of the oxygen and discharge that are consumed can cancel out each other for life.Meanwhile oxygenerator can also
Produce a large amount of oxygen.Therefore, the present invention is the equipment of real green, and an equipment of the invention is equivalent to afforestation hundreds of
Mu.If methane mixed gas input gas distributing system or methane mixed gas are used for internal combustion engine, not because of methane and combustion of hydrogen point
Together.So hydrogen must be separated with methane.It in order to make hydrogen be separated with methane, does not box out, prevents in cathode chamber topmost cathode plate
Only hydrogen enters methane phase room.And in cathode chamber topmost to hydrogen gas outlet is externally provided with, hydrogen is as merchandise sales.
Compared with prior art, life of the invention energy equipment can be realized：Zero consumption conventional energy resource, zero oxygen consumption gas, zero
Pollution；Meanwhile oxygenerator can also produce a large amount of oxygen.Therefore, the present invention is the equipment of real green, and one of the invention
Equipment is equivalent to hundreds of mu of afforestation.
Description of the drawings
Fig. 1 is the system schematic of the present invention.
Specific implementation mode
As shown, air produces the device of methane, by air oxygenerator 1 and methane phase equipment 2 and life energy equipment 3
Composition, which is characterized in that the shunting that the carbon dioxide gas outlet 4 of air oxygenerator 1 passes through pipeline and methane phase equipment 2
The air inlet 6 of room 5 is connected to, and carbon dioxide gas continues to rise out of diffluence room 5 enters methane phase equipment 2 methane phase room 7,
Carbon dioxide generates methane in 7 uphill process of methane phase room, and gas componant has methane, carbon dioxide, hydrogen, oxygen at this time
And other gases, it is referred to as：Methane mixed gas, methane mixed gas continue to rise in methane phase room 7, into methane phase equipment 2
Separation chamber 8, methane mixed gas is discharged from the gas discharge outlet 9 of separation chamber 8, and gas discharge outlet 9 passes through pipeline and life energy
Equipment 3 is connected to, and methane mixed gas, with that can burn (acting) in equipment 3, discharges exhaust gas in life.It can also be most upper in cathode chamber
Portion's cathode plate is not boxed out, and prevents hydrogen from entering methane phase room, and in cathode chamber topmost to being externally provided with hydrogen gas outlet 24, hydrogen
As merchandise sales.
Further include liquefaction pond 10, liquefy pond 10 liquid outlet 11 by pipeline respectively with the rehabilitation of methane backeria poisoning treatment
Center 12 is connected to recovery centre of methane backeria poisoning treatment 13 into liquid port 15, recovery centre of methane backeria poisoning treatment 12 and first
The sludge water outlet 14 of recovery centre of Wan Jun poisoning treatments 13 is connected to diffluence room 5 into the sludge mouth of a river 24 by pipeline, dirty
Muddy water namely for methane strain enters methane phase room 7 from diffluence room 5, continues to rise, into separation chamber 8, dirt of the sludge water from separation chamber 8
The outlet 16 of muddy water is discharged, and outlet 16 is poisoned with recovery centre of methane backeria poisoning treatment 12 and methane backeria respectively by pipeline
Therapy rehabilitation center 13 is connected into the sludge mouth of a river 15, and sludge water namely for methane strain recycles, the rehabilitation of methane backeria poisoning treatment
Center 12 and the top of recovery centre of methane backeria poisoning treatment 13 are respectively equipped with liquid outlet 11, and liquid outlet 11 passes through pipe
Road be connected to liquefaction pond 10 into liquid port respectively, and liquid circulation utilizes zero-emission, recovery centre of methane backeria poisoning treatment 12 He
The top of recovery centre of methane backeria poisoning treatment 13 is additionally provided with biogas outlet 17 respectively, and biogas outlet 17 passes through pipeline and life
Applying flexibly can the connection of equipment 3.
Further include that methane phase equipment 2 is equipped with methane phase room 7, cathode chamber 18, anode chamber 19, anode plate 20 and cathode plate 21 it
Between gap be methane phase room 7, gap between cathode plate 21 and cathode plate 21 is cathode chamber 18, anode plate 20 and anode plate
Gap between 20 is anode chamber 19, and anode chamber 19, cathode chamber 18, methane phase room 7 are referred to as：Three Room are electrolysed, diffluence room 5
The shell of shell top and separation chamber 8 is following, is respectively equipped with trouser legs 22, and three room housings 23 of electrolysis are inserted in the upper of diffluence room 5 below
In the trouser legs 22 on side, the top of three room housings 23 of electrolysis is inserted in the following trouser legs in separation chamber 8.
Claims (3)
1. air produces the device of methane, it is made of with energy equipment (3) air oxygenerator (1) and methane phase equipment (2) and life,
It is characterized in that, the shunting that the carbon dioxide gas outlet (4) of air oxygenerator (1) passes through pipeline and methane phase equipment (2)
The air inlet (6) of room (5) is connected to, and carbon dioxide gas enters the methane phase room of methane phase equipment (2) from the top of diffluence room (5)
(7) in, continue to rise, carbon dioxide generates methane in methane phase room (7) uphill process, and gas componant has methane, two at this time
Carbonoxide, hydrogen, oxygen and other gases, are referred to as：Methane mixed gas, methane mixed gas at the top of methane phase room (7) by entering
The separation chamber (8) of methane phase equipment (2), methane mixed gas are discharged from the gas discharge outlet (9) of separation chamber (8), gas discharge outlet
(9) it is connected to life with energy equipment (3) by pipeline, methane mixed gas burning (acting) in life energy equipment (3), discharge
Exhaust gas can not also box out in cathode chamber topmost cathode plate, prevent hydrogen from entering methane phase room, and in cathode chamber topmost
To hydrogen gas outlet (24) is externally provided with, hydrogen is as merchandise sales.
2. air according to claim 1 produces the device of methane, which is characterized in that further include liquefaction pond (10), liquefaction
The liquid outlet (11) in pond (10) is controlled with recovery centre of methane backeria poisoning treatment (12) and methane backeria poisoning respectively by pipeline
Treat being connected into the sludge mouth of a river (15) for recovery centre (13), recovery centre of methane backeria poisoning treatment (12) and methane backeria poisoning treatment
The sludge water outlet (14) of recovery centre (13) is connected to diffluence room (5) into the sludge mouth of a river (24) by pipeline, sludge water
Namely for methane strain enters methane phase room (7) at the top of diffluence room (5), continues to rise, and sludge water enters from methane phase ceiling portion and divides
From room (8), sludge water is discharged from the outlet (16) of the sludge water of separation chamber (8), outlet (16) by pipeline respectively with first
Recovery centre of Wan Jun poisoning treatments (12) is connected to recovery centre of methane backeria poisoning treatment (13) into the sludge mouth of a river (15), sludge
Water namely for methane strain recycles, recovery centre of methane backeria poisoning treatment (12) and recovery centre of methane backeria poisoning treatment (13)
Top is respectively equipped with liquid outlet (11), and liquid outlet (11) is connected with liquefaction pond (10) into liquid port respectively by pipeline
Logical, liquid circulation utilizes zero-emission, recovery centre of methane backeria poisoning treatment (12) and recovery centre of methane backeria poisoning treatment (13)
Top be additionally provided with biogas outlet (17) respectively, biogas outlet (17) is connected to by pipeline with life with energy equipment (3).
3. air according to claim 1 produces the device of methane, which is characterized in that further include that methane phase equipment (2) is set
There are methane phase room (7), cathode chamber (18), anode chamber (19), the gap between anode plate (20) and cathode plate (21) is methane phase
Room (7), the gap between cathode plate (21) and cathode plate (21) is cathode chamber (18), between anode plate (20) and anode plate (20)
Gap be anode chamber (19), anode chamber (19), cathode chamber (18), methane phase room (7) are referred to as：It is electrolysed three Room, diffluence room (5)
Shell top and separation chamber (8) shell it is following, be respectively equipped with trouser legs (22), the shell (23) for being electrolysed three Room following is inserted in point
The trouser legs (22) of the top of flow chamber (5) is inner, and the top for being electrolysed the shell (23) of three Room is inserted in the following trouser legs in separation chamber (8).
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810185284.4A CN108315233A (en) | 2018-03-01 | 2018-03-01 | Air produces the device of methane |
| CN201811521253.8A CN109554282A (en) | 2018-03-01 | 2018-12-06 | Setting of the oxygenerator in conjunction with methane phase equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810185284.4A CN108315233A (en) | 2018-03-01 | 2018-03-01 | Air produces the device of methane |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108315233A true CN108315233A (en) | 2018-07-24 |
Family
ID=62900407
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810185284.4A Pending CN108315233A (en) | 2018-03-01 | 2018-03-01 | Air produces the device of methane |
| CN201811521253.8A Pending CN109554282A (en) | 2018-03-01 | 2018-12-06 | Setting of the oxygenerator in conjunction with methane phase equipment |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811521253.8A Pending CN109554282A (en) | 2018-03-01 | 2018-12-06 | Setting of the oxygenerator in conjunction with methane phase equipment |
Country Status (1)
| Country | Link |
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| CN (2) | CN108315233A (en) |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009155587A2 (en) * | 2008-06-20 | 2009-12-23 | The Penn State Research Foundation | Electromethanogenic reactor and processes for methane production |
| AT507421B1 (en) * | 2009-04-22 | 2010-05-15 | Joas Elisabeth Mag | PROCESS FOR BIOGENIC SYNTHESIS OF METHANE FROM BIOMASS |
| AU2013294553B2 (en) * | 2012-07-27 | 2016-04-21 | Ffgf Limited | Production of methane |
| CN103966078B (en) * | 2014-05-08 | 2015-12-02 | 中国科学院成都生物研究所 | The device and method of a kind of embedded bio electrolytic hydrogen production and methane |
| CN104176823B (en) * | 2014-07-09 | 2016-08-24 | 浙江大学 | Microorganism electrolysis system and the method integrating biological wastewater treatment and promote methane recovery |
| CN204529850U (en) * | 2015-03-26 | 2015-08-05 | 高节义 | Coal combustion exhaust produces the device of methane |
| CN105861283A (en) * | 2016-04-25 | 2016-08-17 | 高节义 | Miniature methane-producing devices |
| CN106520530A (en) * | 2016-05-25 | 2017-03-22 | 高节义 | Methane bacterium poisoning treatment and rehabilitation center arrangement |
| CN106635754A (en) * | 2016-07-05 | 2017-05-10 | 高节义 | Combined methane production apparatus |
| CN106435637A (en) * | 2016-11-17 | 2017-02-22 | 高节义 | System setting for self supply of energy source and oxygen and cyclic utilization and zero emission of exhaust gas of boiler internal combustion engine |
| CN106947688B (en) * | 2017-02-16 | 2019-03-19 | 重庆大学 | Microorganism/photoelectric coupling reduction carbon dioxide methane phase System and method for |
| CN106835186A (en) * | 2017-03-02 | 2017-06-13 | 高节义 | It is electrolysed the method and device that methane is produced in three Room |
| CN206929758U (en) * | 2017-06-28 | 2018-01-26 | 高节义 | Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission |
-
2018
- 2018-03-01 CN CN201810185284.4A patent/CN108315233A/en active Pending
- 2018-12-06 CN CN201811521253.8A patent/CN109554282A/en active Pending
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| Publication number | Publication date |
|---|---|
| CN109554282A (en) | 2019-04-02 |
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Application publication date: 20180724 |