CN109401925A - It is electrolysed the shell setting of three Room - Google Patents
It is electrolysed the shell setting of three Room Download PDFInfo
- Publication number
- CN109401925A CN109401925A CN201710720876.7A CN201710720876A CN109401925A CN 109401925 A CN109401925 A CN 109401925A CN 201710720876 A CN201710720876 A CN 201710720876A CN 109401925 A CN109401925 A CN 109401925A
- Authority
- CN
- China
- Prior art keywords
- room
- baffle
- slot
- sludge water
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 57
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 56
- 239000010802 sludge Substances 0.000 claims abstract description 48
- 238000000926 separation method Methods 0.000 claims abstract description 21
- 239000004744 fabric Substances 0.000 claims abstract description 12
- 238000009434 installation Methods 0.000 claims abstract description 7
- 238000002485 combustion reaction Methods 0.000 claims description 12
- 238000005868 electrolysis reaction Methods 0.000 claims description 12
- 239000007789 gas Substances 0.000 description 43
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 8
- 230000000694 effects Effects 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- -1 oxonium ion Chemical class 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000002560 therapeutic procedure Methods 0.000 description 1
- 239000002912 waste gas Substances 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
- C12M1/00—Apparatus for enzymology or microbiology
- C12M1/107—Apparatus for enzymology or microbiology with means for collecting fermentation gases, e.g. methane
-
- 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
-
- 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
It is electrolysed the shell setting of three Room, the shell for being electrolysed three Room is made of front and rear baffle (1) and both ends baffle (2), it is characterized in that, front and rear baffle (1) is respectively equipped with water inlet (3) and gas delivery port (4), the bottom of front and rear baffle (1) is equipped with sludge water exhaust gas diffluence room (5), the top of front and rear baffle (1) is equipped with sludge water and gas separation chamber (8), separation chamber (8) is equipped with gas delivery port (9), separation chamber (8) is additionally provided with sludge water outlet (13), both ends baffle (2) is respectively equipped with slot (18I), (18II), slot (18I) the installation cathode plate and screen cloth of both ends baffle (2), slot (18II) the installation anode plate and screen cloth of both ends baffle (2), gap is methane phase room (19) between slot (18I) and slot (18II), slot Gap is cathode chamber (20) between 18II and front apron, and gap is anode chamber (21) between slot 18II and rear baffle.
Description
Technical field
The present invention relates to the device that methane is produced in a kind of three Room of electrolysis, especially a kind of shell setting for being electrolysed three Room.
Background technique
Currently, the device that methane is produced in three Room of electrolysis designs a good shell not yet.Therefore, a kind of electrolysis is designed
The shell of three Room is arranged, and is the current technical issues that need to address.
Summary of the invention
Technical problem to be solved by the invention is to provide the shells that three Room of electrolysis of methane device is produced in a kind of three Room of electrolysis
Body setting.
The present invention the technical solution to solve the technical problem is that:
It is electrolysed the shell setting of three Room, the shell of three Room of electrolysis is made of front and rear baffle and both ends baffle.Front and rear baffle point
It She You not water inlet and gas delivery port.The bottom of front and rear baffle is equipped with sludge water exhaust gas diffluence room, sludge water exhaust gas diffluence room
It is connected to methane phase room.Diffluence room is equipped with into the sludge mouth of a river and into exhaust outlet.The effect of diffluence room: by sludge water and boiler internal combustion
The exhaust gas of machine discharge is diverted to each methane phase room.The top of front and rear baffle be equipped with sludge water and gas separation chamber, sludge water and
Gas separation chamber is connected to methane phase room.Separation chamber is equipped with gas delivery port, the air inlet of gas delivery port and boiler internal combustion engine
Connection.Baffle is equipped between the inside and methane phase room of gas delivery port.The effect of baffle: gas is stopped to flow directly into gas defeated
Outlet makes gas dispersion, flow velocity slow down, hereby, it is achieved that the moisture that gas carries is fallen, forces gas and sludge water content
From the moisture that reduction gas carries.Separation chamber is additionally provided with sludge water outlet, the sludge water of sludge water outlet and methane-generating pit into
Mouth connection.The sludge water outlet of methane-generating pit is connected to diffluence room into the sludge mouth of a river.Sewage pump is equipped with inside methane-generating pit.Sewage
The effect of pump: first is that the sludge water in stirring methane-generating pit；Second is that sludge water is discharged.Methane-generating pit is additionally provided with biogas outlet,
Outlet is connected to the air inlet of boiler internal combustion engine.The biogas boiler of feeding combustion in IC engine acting that methane-generating pit generates.Both ends baffle
It is respectively equipped with slot 18I, 18II, the slot 18I installation cathode plate and screen cloth of both ends baffle, the slot 18II of both ends baffle installs anode plate
And screen cloth, gap is methane phase room between slot 18I and slot 18II, and gap is cathode chamber, slot 18II between slot 18II and front apron
Gap is anode chamber between rear baffle.The effect of the slot of both ends baffle: fixed anode plate and screen cloth, fixed negative pole plate and net
Cloth.The bottom of front and rear baffle and both ends baffle is equipped with sludge water exhaust gas diffluence room, and the top of front and rear baffle and both ends baffle is equipped with
Sludge water and gas separation chamber, above diffluence room and separation chamber are equipped with baffle separately below.Baffle effect: installation diffluence room,
When separation chamber is connected with front and rear baffle, both ends baffle, baffle is respectively inserted in the outside of cathode plate, anode plate, prevents anode plate, yin
Pole plate is displaced outwardly.Meanwhile preventing sludge water, gas from flowing to anode chamber, cathode chamber.
Sludge water (methane strain) in methane-generating pit: 1, being extracted into sludge water exhaust gas diffluence room with sewage pump by working principle,
The exhaust gas of boiler engine exhaust is transported to diffluence room simultaneously, sludge water, exhaust gas are diverted to each methane phase room, sludge
Water, exhaust gas rise, and the hydrogen ion generated with water electrolysis meets, the hydrogen ion that the carbon dioxide and water electrolysis in exhaust gas generate,
Under the action of methane backeria, synthesizing methane.Methane gas rises, and is discharged from gas discharge outlet, is transported to boiler combustion in IC engine and does
Function discharges exhaust gas and water.Waste gas circulation utilizes zero-emission.
2, pure water or electrolysis water are transported to anode chamber, are ionized through anode plate, generate hydrogen ion water, hydrogen ion water passes through sun
The hole of pole plate penetrates screen cloth, and into methane phase room, hydrogen ion meets with the carbon dioxide in exhaust gas, closes under the action of methane backeria
At methane.The hydrogen ion slipped through the net, under cathode plate attraction, into cathode chamber.Hydrogen ion generates hydrogen, hydrogen in conjunction with hydrogen ion
Gas rises, and is discharged from gas discharge outlet, is transported to the acting of boiler combustion in IC engine.
3, pure water or electrolysis water are transported to cathode chamber, are ionized through cathode plate, generate oxonium ion water, oxonium ion water passes through yin
The hole of pole plate penetrates screen cloth, into methane phase room, under the attraction of anode plate, into anode chamber.Oxonium ion is combined with oxonium ion,
Oxygen is generated, oxygen rises, and is discharged from gas discharge outlet, is transported to the acting of boiler internal combustion engine combustion supporting.
4, oxygen can make methane backeria be poisoned, or even dead.The methane backeria of poisoning is transported to methane-generating pit, therapy rehabilitation, first
Alkane bacterium recycles.
Compared with prior art, the present invention can be easily installed anode plate or cathode plate fixation, and design is more closed
Reason.
Detailed description of the invention
Fig. 1 is schematic structural view of the invention；
Fig. 2 is 2 main view of Fig. 1；
Fig. 3 is 1 sectional view of Fig. 1.
Specific embodiment
It is electrolysed the shell setting of three Room, the shell of three Room of electrolysis is made of front and rear baffle 1 and both ends baffle 2.Front and rear baffle 1
It is respectively equipped with water inlet 3 and gas delivery port 4, the bottom of front and rear baffle 1 is equipped with sludge water exhaust gas diffluence room 5, sludge water exhaust gas
Diffluence room 5 is connected to methane phase room 19, and diffluence room 5 is equipped with into the sludge mouth of a river 6 and into exhaust outlet 7, and the top of front and rear baffle 1 is equipped with
Sludge water and gas separation chamber 8, sludge water and gas separation chamber 8 are connected to methane phase room 19, and it is defeated that gas separation chamber 8 is equipped with gas
Outlet 9, gas delivery port 9 is connected to the air inlet 11 of boiler internal combustion engine 10, between the inside and methane phase room of gas delivery port 9
Equipped with baffle 12, gas separation chamber 8 is additionally provided with sludge water outlet 13, the sludge water of sludge water outlet 13 and methane-generating pit 14 into
Mouthfuls 15 are connected to, the sludge water outlet 16 of methane-generating pit 14 and being connected into the sludge mouth of a river 6 for diffluence room 5, and methane-generating pit 14 is additionally provided with natural pond
Gas outlet 17, outlet 17 are connected to the air inlet 11 of boiler internal combustion engine 10, and both ends baffle 2 is respectively equipped with slot 18I, 18II,
The slot 18I installation cathode plate and screen cloth of both ends baffle 2, the slot 18II installation anode plate and screen cloth, slot 18I and slot of both ends baffle 2
Gap is methane phase room 19 between 18II, and gap is cathode chamber 20 between slot 18II and front apron, between slot 18II and rear baffle
Gap is anode chamber 21.The bottom of front and rear baffle 1 and both ends baffle 2 is equipped with sludge water exhaust gas diffluence room 5, front and rear baffle 1 and two
The top of first speed plate 2 be equipped with sludge water and gas separation chamber 8, diffluence room 5 above and separation chamber 8 separately below equipped with baffle 21,
22。
Claims (1)
1. being electrolysed the shell setting of three Room, the shell of three Room of electrolysis is made of front and rear baffle (1) and both ends baffle (2), feature
It is, front and rear baffle (1) is respectively equipped with water inlet (3) and gas delivery port (4), and the bottom of front and rear baffle (1) is equipped with sludge water
Exhaust gas diffluence room (5), sludge water exhaust gas diffluence room (5) are connected to methane phase room (19), and diffluence room (5) is equipped with into the sludge mouth of a river
(6) and into exhaust outlet (7), the top of front and rear baffle (1) is equipped with sludge water and gas separation chamber (8), sludge water and gas separation
Room (8) is connected to methane phase room (19), and separation chamber (8) are equipped with gas delivery port (9), gas delivery port (9) and boiler internal combustion engine
(10) air inlet (11) connection, is equipped with baffle (12) between the inside and methane phase room of gas delivery port (9), separation chamber (8)
It is additionally provided with sludge water outlet (13), sludge water outlet (13) is connected to the sludge water inlet (15) of methane-generating pit (14), biogas
The sludge water outlet (16) in pond (14) is connected to diffluence room (5) into the sludge mouth of a river (6), and methane-generating pit (14) is additionally provided with biogas row
It exports (17), outlet (17) is connected to the air inlet (11) of boiler internal combustion engine (10), and both ends baffle (2) is respectively equipped with slot
(18I), (18II), slot (18I) the installation cathode plate and screen cloth of both ends baffle (2), the slot (18II) of both ends baffle (2) install sun
Pole plate and screen cloth, gap is methane phase room (19) between slot (18I) and slot (18II), and gap is between slot (18II) and front apron
Cathode chamber (20), gap is anode chamber (21), the bottom of front and rear baffle (1) and both ends baffle (2) between slot (18II) and rear baffle
Portion is equipped with sludge water exhaust gas diffluence room (5), and front and rear baffle (1) is equipped with sludge water with the top of both ends baffle (2) and gas separates
Room (8), diffluence room (5) are equipped with baffle (22), (23) with separation chamber (8) above separately below.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710720876.7A CN109401925A (en) | 2017-08-15 | 2017-08-15 | It is electrolysed the shell setting of three Room |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710720876.7A CN109401925A (en) | 2017-08-15 | 2017-08-15 | It is electrolysed the shell setting of three Room |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109401925A true CN109401925A (en) | 2019-03-01 |
Family
ID=65463225
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710720876.7A Pending CN109401925A (en) | 2017-08-15 | 2017-08-15 | It is electrolysed the shell setting of three Room |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109401925A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009072778A (en) * | 2007-04-13 | 2009-04-09 | Masaaki Arai | Electrolytic water producing device and method, and electrolytic water |
| CN102395709A (en) * | 2009-02-17 | 2012-03-28 | 麦卡利斯特技术有限责任公司 | Apparatus and method for gas capture during electrolysis |
| CN104593143A (en) * | 2014-12-29 | 2015-05-06 | 胡发庭 | Method for preparing camellia oil capsules at low temperature and deodorization electrolysis equipment thereof |
| 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 |
| CN207079228U (en) * | 2017-08-15 | 2018-03-09 | 高节义 | The housing for being electrolysed three Room is set |
-
2017
- 2017-08-15 CN CN201710720876.7A patent/CN109401925A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009072778A (en) * | 2007-04-13 | 2009-04-09 | Masaaki Arai | Electrolytic water producing device and method, and electrolytic water |
| CN102395709A (en) * | 2009-02-17 | 2012-03-28 | 麦卡利斯特技术有限责任公司 | Apparatus and method for gas capture during electrolysis |
| CN104593143A (en) * | 2014-12-29 | 2015-05-06 | 胡发庭 | Method for preparing camellia oil capsules at low temperature and deodorization electrolysis equipment thereof |
| 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 |
| CN207079228U (en) * | 2017-08-15 | 2018-03-09 | 高节义 | The housing for being electrolysed three Room is set |
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| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Gao Jieyi Document name: Notice of First Examination Opinion |
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| DD01 | Delivery of document by public notice | ||
| DD01 | Delivery of document by public notice |
Addressee: Gao Jieyi Document name: Deemed withdrawal notice |
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| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20190301 |