CN109554282A - Setting of the oxygenerator in conjunction with methane phase equipment - Google Patents
Setting of the oxygenerator in conjunction with methane phase equipment Download PDFInfo
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- CN109554282A CN109554282A CN201811521253.8A CN201811521253A CN109554282A CN 109554282 A CN109554282 A CN 109554282A CN 201811521253 A CN201811521253 A CN 201811521253A CN 109554282 A CN109554282 A CN 109554282A
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- Prior art keywords
- methane
- room
- equipment
- methane phase
- outlet
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 368
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 48
- 238000000926 separation method Methods 0.000 claims abstract description 32
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 24
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 8
- 239000007789 gas Substances 0.000 claims description 50
- 208000005374 Poisoning Diseases 0.000 claims description 48
- 231100000572 poisoning Toxicity 0.000 claims description 48
- 230000000607 poisoning effect Effects 0.000 claims description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 43
- 238000011084 recovery Methods 0.000 claims description 42
- 239000010802 sludge Substances 0.000 claims description 33
- 239000001257 hydrogen Substances 0.000 claims description 21
- 229910052739 hydrogen Inorganic materials 0.000 claims description 21
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 16
- 239000001301 oxygen Substances 0.000 claims description 16
- 229910052760 oxygen Inorganic materials 0.000 claims description 16
- 238000005868 electrolysis reaction Methods 0.000 claims description 11
- 150000002431 hydrogen Chemical class 0.000 claims description 5
- 241000894006 Bacteria Species 0.000 claims description 2
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 11
- -1 oxonium ion Chemical class 0.000 description 5
- 238000009395 breeding Methods 0.000 description 3
- 230000001488 breeding effect Effects 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000036284 oxygen consumption Effects 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000002860 competitive effect Effects 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000002560 therapeutic procedure Methods 0.000 description 1
Classifications
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
Abstract
Setting of the oxygenerator in conjunction with methane phase equipment, it is made of air oxygenerator (1) and methane phase equipment (2) and energy for life equipment (3), 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) enter 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 energy for life equipment (3), methane mixed gas is in energy for life equipment (3) it burns (acting) in, discharges exhaust gas.
Description
Technical field
The present invention relates to the device that a kind of air produces methane, especially a kind of oxygenerator setting in conjunction with methane phase equipment
It sets.
Background technique
Currently, China and world's air produce the device technique or blank of methane.Therefore, a kind of oxygenerator of researching and designing
Setting in conjunction with methane phase equipment is the current technical issues that need to address.
Summary of the invention
The technical problems to be solved by the present invention are: setting technical solution of the oxygenerator in conjunction with methane phase equipment.
The present invention the technical solution to solve the technical problem is that:
Setting of the oxygenerator in conjunction with methane phase equipment, by air oxygenerator and methane phase equipment and energy for life equipment group
At.The oxygen that air oxygenerator is produced is sold to user as commodity.The carbon dioxide gas that air oxygenerator is produced
The diffluence room of methane phase equipment is pipelined to from outlet.Carbon dioxide gas enters methane phase equipment from diffluence room
In methane phase room, continue to rise.Carbon dioxide generates methane in the uphill process of methane phase room.At this time gas componant have methane,
Carbon dioxide, hydrogen, oxygen and other gases are referred to as are as follows: methane mixed gas, on methane mixed gas continues in methane phase room
It rises, into the separation chamber of methane phase equipment, methane mixed gas is discharged from the gas discharge outlet of separation chamber, and gas discharge outlet passes through pipe
Road is transported to energy for life equipment, and methane mixed gas burns (acting) in energy for life equipment, discharges exhaust gas.Can also
Cathode chamber topmost cathode plate is not boxed out, and prevents hydrogen from entering methane phase room, and defeated to hydrogen is externally provided in cathode chamber topmost
Outlet.After hydrogen output, store, hydrogen is as merchandise sales.
As a preferred solution of the present invention, further include liquefaction pond, fill up organic matter in liquefaction pond first, fill
Water is dissolved into organic matter in 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, methane backeria poisoning treatment 12 and recovery centre, methane backeria poisoning treatment 13,
The sludge water of recovery centre, methane backeria poisoning treatment 12 and recovery centre, methane backeria poisoning treatment 13 is discharged from outlet, sludge water
It is pipelined to diffluence room, sludge water namely for methane strain enters methane phase room from diffluence room, continues to rise, into separation
Room, sludge water from the outlet discharge of the sludge water of separation chamber, outlet by pipeline respectively with the rehabilitation of methane backeria poisoning treatment
Center 12 is connected to recovery centre, methane backeria poisoning treatment 13 into the sludge mouth of a river (15), sludge water namely for methane strain circulation benefit
With.In recovery centre, methane backeria poisoning treatment (12) and recovery centre, methane backeria poisoning treatment 13, because the specific gravity of sludge is greater than 1,
Sludge sinks, in bottom；Top is supernatant.Recovery centre, methane backeria poisoning treatment 12 and recovery centre, methane backeria poisoning treatment
13 top is respectively equipped with liquid outlet, and liquid outlet is connected to liquefaction pond into liquid port respectively by pipeline, liquid
Recycle zero-emission.The top of recovery centre, methane backeria poisoning treatment 12 and recovery centre, methane backeria poisoning treatment 13 difference
It is additionally provided with biogas outlet, biogas outlet is connected to by pipeline with energy for life equipment.Recovery centre, methane backeria poisoning treatment
12 and recovery centre, methane backeria poisoning treatment 13 effect: first by sludge water namely for methane strain inject the rehabilitation of methane backeria poisoning treatment
In center；Also in methane phase room, first is that the hydrogen ion that carbon dioxide and water electrolysis generate, synthesizes under the action of methane backeria
Methane, meanwhile, discharge oxygen；Second is that the oxonium ion that cathode plate generates.Oxygen and oxonium ion can inhibit methane backeria movable, even
Keep methane backeria dead.Aerobic bacteria in recovery centre, methane backeria poisoning treatment 12 eats up the oxygen of methane backeria carrying, makes methane backeria
Rehabilitation.When the quantity of methane backeria death is greater than the quantity of breeding, i.e., the methane mixed gas outlet in separation chamber is equipped with methane
Table, when methane table shows that methane content gradually decreases, it was demonstrated that: the death rate of methane backeria is greater than breeding potential.At this moment methane backeria is closed
Recovery centre, poisoning treatment 12.Start recovery centre, methane backeria poisoning treatment 13, is taken out from recovery centre, methane backeria poisoning treatment 13
Sludge water is taken to inject diffluence room, sludge water enters methane phase room from diffluence room, and sludge water enters separation chamber from methane phase ceiling portion,
It is discharged from outlet, automatic back flow to recovery centre, methane backeria poisoning treatment 13, sludge water circulation use zero-emission.At this point, from
The pond extraction organic water that liquefies injects recovery centre, methane backeria poisoning treatment 12, and organic water is in recovery centre, methane backeria poisoning treatment 12
It is interior, rise, be discharged from top outlet, overflows to liquefaction pond, organic water circulation use zero-emission.In this course, methane
Bacterium obtains breeding and grows body key.Recovery centre, methane backeria poisoning treatment 12 and the exchange of recovery centre, methane backeria poisoning treatment 13 make
With.But recovery centre, methane backeria poisoning treatment 12 and recovery centre, methane backeria poisoning treatment 13, when working at the same time, working performance
It is different.
It as a preferred solution of the present invention, further include that methane phase equipment is equipped with methane phase room, cathode chamber, anode chamber,
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 are as follows: three Room of electrolysis.Under the shell top of diffluence room and the shell of separation chamber
Side, is respectively equipped with trousers letter, in the trouser legs of the shell top that is inserted in diffluence room below of three Room of electrolysis.It is electrolysed the upper of the shell of three Room
While being inserted in the following trouser legs in separation chamber, so that three Room of electrolysis, diffluence room, separation chamber is fixed together, form methane phase equipment.
Working principle: the carbon dioxide of oxygenerator production, by air pump, the diffluence room of pipeline to methane phase equipment,
Carbon dioxide gas rises under the action of pump pressure, respectively enters in each methane phase room, rises rapidly from diffluence room, into point
From room, continue to rise, be discharged from separation chamber's top gas outlet；There are also the sludge in recovery centre, methane backeria poisoning treatment
Water is infused the sludge water in recovery centre, methane backeria poisoning treatment into diffluence room by sewage pump, under the action of pump pressure, on
It rises, respectively enters each methane phase room, continue to rise, into separation chamber, because sludge water is than great, from separation chamber's bottom discharge outlet
Discharge；At this point, water electrolyzer is started to work, anode chamber and cathode chamber hydraulic pressure make cathode chamber and sun greater than the hydraulic pressure of methane phase room
Water in pole room in the presence of hydraulic pressure, flows to methane phase room automatically.Anode plate generate hydrogen ion, anode chamber formed hydrogen from
Sub- water, first is that the hydraulic pressure of the hydrogen ion water of anode chamber is greater than the pressure of the sludge water of methane phase room, work of the hydrogen ion water in hydraulic pressure
Under, methane phase room is flowed to by asymmetric diaphragm automatically.Second is that hydrogen ion cathode plate attraction under, by asymmetry electrolysis every
Film is into cathode plate transfer process, when passing by methane phase room.Hydrogen ion in hydrogen ion water methane phase room and carbon dioxide with
Methane backeria in sludge water meets, and carbon dioxide and hydrogen ion are under the action of methane backeria, synthesizing methane.Meanwhile also discharging oxygen
Gas.Methane gas and oxygen rise, and enter separation chamber from methane phase ceiling portion, are discharged from the gas discharge outlet of separation chamber；It slips through the net
Hydrogen ion enter cathode chamber, hydrogen ion in conjunction with hydrogen ion, generate hydrogen, hydrogen rise, from cathode chamber topmost through yin
The hole of pole plate and electrolyte membrane enter separation chamber from methane phase ceiling portion, the gas discharge outlet from separation chamber into methane phase room
Discharge；The oxonium ion that cathode plate generates shifts, oxonium ion and oxonium ion in anode chamber under the attraction of anode plate to anode chamber
In conjunction with oxygen is generated, oxygen rises, hole and electrolyte membrane from anode chamber's topmost through anode plate, into methane phase room, from
Methane phase ceiling portion enters separation chamber, is discharged from the gas discharge outlet of separation chamber.The gas being discharged from the gas discharge outlet of separation chamber
Body has: the gases such as methane, oxygen, hydrogen, carbon dioxide, is referred to as are as follows: methane mixed gas.Methane mixed gas is pipelined to
Energy for life equipment is burnt (acting), and carbon dioxide and water are discharged.Energy for life equipment: cooking stove, boiler, water heater,
Family heating system etc..Energy for life equipment can be realized: zero consumption conventional energy resource, zero oxygen consumption gas, no pollution.It is being electrolysed three Room
During producing methane, the oxygen of release and the oxygen of generation and carbon dioxide conversion are methane and energy for life equipment in work
When making, the carbon dioxide of consumed oxygen and discharge can cancel out each other.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 the several hundred mus of afforestation.If methane blended
Gas inputs gas distributing system or methane mixed gas is used for internal combustion engine, because methane is different from combustion of hydrogen point.So hydrogen and methane
It must separate.In order to separate hydrogen with methane, does not box out in cathode chamber topmost cathode plate, prevent hydrogen from entering 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, energy for life equipment of the invention 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 the several hundred mus of afforestation.
Detailed description of the invention
Fig. 1 is system schematic of the invention.
Specific embodiment
As shown, setting of the oxygenerator in conjunction with methane phase equipment, by air oxygenerator 1 and methane phase equipment 2 and life
It applies flexibly energy equipment 3 to form, which is characterized in that the carbon dioxide gas outlet 4 of air oxygenerator 1 is set by pipeline and methane phase
The air inlet 6 of standby 2 diffluence room 5 is connected to, carbon dioxide gas out of, diffluence room 5 enters methane phase equipment 2 methane phase room 7,
Continue to rise, carbon dioxide in 7 uphill process of methane phase room, generate methane, at this time gas componant have methane, carbon dioxide,
Hydrogen, oxygen and other gases are referred to as are as follows: methane mixed gas, methane mixed gas continue to rise in methane phase room 7, into production
The separation chamber 8 of methane equipment 2, methane mixed gas from the gas discharge outlet 9 of separation chamber 8 be discharged, gas discharge outlet 9 by pipeline with
Energy for life equipment 3 is connected to, and methane mixed gas burns (acting) in energy for life equipment 3, discharges exhaust gas.It can also be in yin
Pole room topmost cathode plate is not boxed out, and prevents hydrogen from entering methane phase room, and is exported in cathode chamber topmost to hydrogen is externally provided with
Mouth 24, hydrogen is as merchandise sales.
Further include liquefaction pond 10, liquefaction pond 10 liquid outlet 11 by pipeline respectively with the rehabilitation of methane backeria poisoning treatment
Center 12 is connected to recovery centre, methane backeria poisoning treatment 13 into liquid port 15, recovery centre, methane backeria poisoning treatment 12 and first
The sludge water outlet 14 of recovery centre, Wan Jun poisoning treatment 13 is connected to by pipeline and diffluence room 5 into the sludge mouth of a river 24, dirt
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, 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, 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, methane backeria poisoning treatment 12 He
The top of recovery centre, 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 are as follows: three Room of electrolysis, 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.
Methane phase equipment and recovery centre, methane backeria poisoning treatment are components of the invention, rather than the present application is created
It makes, so summary, summary is in order to illustrate working principle of the present invention.
Specific implementation, by owner in market competitive bidding, company winning a bid specification, Figure of description and tool according to the present invention
Body embodiment chooses establishment to market.Company winning a bid according to the present invention specification, Figure of description, specific embodiment and
The product description of various components is constructed, installation and debugging, trial operation, operation and operational management.
Claims (3)
1. setting of the oxygenerator in conjunction with methane phase equipment is set by air oxygenerator (1) and methane phase equipment (2) and energy for life
Standby (3) form, which is characterized in that the carbon dioxide gas outlet (4) of air oxygenerator (1) passes through pipeline and methane phase equipment
(2) air inlet (6) of diffluence room (5) is connected to, and carbon dioxide gas enters methane phase equipment (2) from the top of diffluence room (5)
Methane phase room (7) in, continue to rise, carbon dioxide in methane phase room (7) uphill process, generate methane, at this time gas at
Dividing has methane, carbon dioxide, hydrogen, oxygen and other gases, is referred to as are as follows: methane mixed gas, methane mixed gas is by methane phase room
(7) top enters the separation chamber (8) of methane phase equipment (2), and methane mixed gas is discharged from the gas discharge outlet (9) of separation chamber (8),
Gas discharge outlet (9) is connected to by pipeline with energy for life equipment (3), methane mixed gas burning in energy for life equipment (3)
(acting) discharges exhaust gas, can not also box out in cathode chamber topmost cathode plate, prevent hydrogen from entering methane phase room, and
Cathode chamber topmost is to hydrogen gas outlet (24) are externally provided with, and hydrogen is as merchandise sales.
2. setting of the oxygenerator according to claim 1 in conjunction with methane phase equipment, which is characterized in that further include liquefaction pond
(10), liquefy pond (10) liquid outlet (11) by pipeline respectively with recovery centre, methane backeria poisoning treatment (12) and methane
Recovery centre, bacterium poisoning treatment (13) is connected into the sludge mouth of a river (15), recovery centre, methane backeria poisoning treatment (12) and methane backeria
The sludge water outlet (14) of recovery centre, poisoning treatment (13) by pipeline and diffluence room (5) into the sludge mouth of a river (24) even
Logical, sludge water namely for methane strain enters methane phase room (7) at the top of diffluence room (5), continues to rise, and sludge water is from methane phase ceiling
Portion enters separation chamber (8), and sludge water is discharged from the outlet (16) of the sludge water of separation chamber (8), and outlet (16) passes through pipeline
Respectively with recovery centre, methane backeria poisoning treatment (12) and recovery centre, methane backeria poisoning treatment (13) into the sludge mouth of a river (15)
Connection, sludge water namely for methane strain recycle, recovery centre, methane backeria poisoning treatment (12) and the rehabilitation of methane backeria poisoning treatment
The top at center (13) is respectively equipped with liquid outlet (11), liquid outlet (11) by pipeline respectively with liquefaction pond (10)
It is connected into liquid port, liquid circulation utilizes zero-emission, recovery centre, methane backeria poisoning treatment (12) and methane backeria poisoning treatment health
The top of multiple center (13) is additionally provided with biogas outlet (17) respectively, and biogas outlet (17) passes through pipeline and energy for life equipment
(3) it is connected to.
3. setting of the oxygenerator according to claim 1 in conjunction with methane phase equipment, which is characterized in that further include methane phase
Equipment (2) is equipped with methane phase room (7), cathode chamber (18), anode chamber (19), the gap between anode plate (20) and cathode plate (21)
For methane phase room (7), the gap between cathode plate (21) and cathode plate (21) is cathode chamber (18), anode plate (20) and anode plate
(20) gap between is anode chamber (19), and anode chamber (19), cathode chamber (18), methane phase room (7) are referred to as are as follows: three Room of electrolysis,
Diffluence room (5) in the top for being electrolysed three Room, is respectively equipped with trouser legs (22) in electrolysis the following of three Room, separation chamber (8), is electrolysed three Room
Shell (23) top that is inserted in diffluence room (5) below trouser legs (22) it is inner, the top for being electrolysed the shell (23) of three Room is inserted in point
In the trouser legs following from room (8).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2018101852844 | 2018-03-01 | ||
| CN201810185284.4A CN108315233A (en) | 2018-03-01 | 2018-03-01 | Air produces the device of methane |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109554282A true CN109554282A (en) | 2019-04-02 |
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 Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810185284.4A Pending CN108315233A (en) | 2018-03-01 | 2018-03-01 | Air produces the device of methane |
Country Status (1)
| Country | Link |
|---|---|
| CN (2) | CN108315233A (en) |
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| CN106520530A (en) * | 2016-05-25 | 2017-03-22 | 高节义 | Methane bacterium poisoning treatment and rehabilitation center arrangement |
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| 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 |
| CN106947688A (en) * | 2017-02-16 | 2017-07-14 | 重庆大学 | Microorganism/photoelectric coupling reduces the System and method for of carbon dioxide methane phase |
| 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 |
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2018
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- 2018-12-06 CN CN201811521253.8A patent/CN109554282A/en active Pending
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