CN108468063A - The system and device that internal combustion engine is combined with three Room of electrolysis - Google Patents
The system and device that internal combustion engine is combined with three Room of electrolysis Download PDFInfo
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- CN108468063A CN108468063A CN201810473433.7A CN201810473433A CN108468063A CN 108468063 A CN108468063 A CN 108468063A CN 201810473433 A CN201810473433 A CN 201810473433A CN 108468063 A CN108468063 A CN 108468063A
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- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 49
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 46
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 186
- 239000007789 gas Substances 0.000 claims abstract description 103
- 238000000926 separation method Methods 0.000 claims abstract description 25
- 239000002912 waste gas Substances 0.000 claims abstract description 10
- 238000007667 floating Methods 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 100
- 239000010802 sludge Substances 0.000 claims description 43
- 208000005374 Poisoning Diseases 0.000 claims description 13
- 231100000572 poisoning Toxicity 0.000 claims description 13
- 230000000607 poisoning effect Effects 0.000 claims description 13
- 238000011084 recovery Methods 0.000 claims description 13
- 239000001257 hydrogen Substances 0.000 claims description 11
- 229910052739 hydrogen Inorganic materials 0.000 claims description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 9
- 239000003792 electrolyte Substances 0.000 claims description 9
- 239000012528 membrane Substances 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 4
- 230000029087 digestion Effects 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims description 3
- 150000002431 hydrogen Chemical class 0.000 claims description 3
- 239000000618 nitrogen fertilizer Substances 0.000 claims description 3
- 239000010815 organic waste Substances 0.000 claims description 3
- 239000002686 phosphate fertilizer Substances 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 239000002737 fuel gas Substances 0.000 claims 1
- 239000008246 gaseous mixture Substances 0.000 claims 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 18
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 12
- 229910002092 carbon dioxide Inorganic materials 0.000 description 9
- 239000001569 carbon dioxide Substances 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 7
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- -1 oxonium ion Chemical class 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- 241000208340 Araliaceae Species 0.000 description 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 1
- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000009189 diving Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000002560 therapeutic procedure Methods 0.000 description 1
Classifications
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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
-
- 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
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B43/00—Engines characterised by operating on gaseous fuels; Plants including such engines
- F02B43/10—Engines or plants characterised by use of other specific gases, e.g. acetylene, oxyhydrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M26/00—Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02M—SUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
- F02M26/00—Engine-pertinent apparatus for adding exhaust gases to combustion-air, main fuel or fuel-air mixture, e.g. by exhaust gas recirculation [EGR] systems
- F02M26/13—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories
- F02M26/22—Arrangement or layout of EGR passages, e.g. in relation to specific engine parts or for incorporation of accessories with coolers in the recirculation passage
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B43/00—Engines characterised by operating on gaseous fuels; Plants including such engines
- F02B43/10—Engines or plants characterised by use of other specific gases, e.g. acetylene, oxyhydrogen
- F02B2043/103—Natural gas, e.g. methane or LNG used as a fuel
-
- 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
-
- 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/30—Use of alternative fuels, e.g. biofuels
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
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- Molecular Biology (AREA)
- General Chemical & Material Sciences (AREA)
- Biomedical Technology (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Sustainable Development (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Inorganic Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The system and device that internal combustion engine is combined with three Room of electrolysis,It is made of internal combustion engine (1) and electrolysis three rooms (2),It is characterized in that,The outlet port (3) of internal combustion engine (1) is connected to cover-floating type gas holder (4) into exhaust outlet (5),The outlet port (6) of cover-floating type gas holder (4) is connected to cooler (7) into exhaust outlet (8),The outlet port (9) of cooler (7) is connected to the diffluence room (10) of electrolysis three rooms (2) into exhaust outlet (11),Exhaust gas ascends into methane phase room (12),Generate methane mixed gas,Ascend into separation chamber (13),Methane mixed gas outlet (14) is connected to the air inlet (17) of methane mixed gas gas holder (16),The gas discharge outlet (18) of methane mixed gas gas holder (16) is connected to the air inlet (19) of internal combustion engine (1),Internal combustion engine realizes that waste gas circulation utilizes zero-emission.
Description
Technical field
The present invention relates to the system and devices that a kind of internal combustion engine is combined with three Room of electrolysis.
Background technology
Currently, internal combustion engine can't realize that waste gas circulation utilizes zero-emission.Therefore, it is necessary to design a kind of internal combustion engine with
It is electrolysed the system and device of three Room combination, engine exhaust gas is made to recycle zero-emission, zero consumption commercial energy.
Invention content
Technical problem to be solved by the invention is to provide the system and devices that a kind of internal combustion engine is combined with three Room of electrolysis
Technical solution.
The present invention the technical solution to solve the technical problem is that：
Internal combustion engine does not newly have air cleaner, not into air scoop in internal combustion engine；Combustion in IC engine methane blended
Gas, namely for methane gas.Because methane gas is different from the ignition point of hydrogen gas.Therefore, it is necessary to the hydrogen in methane mixed gas
It separates, makes combustion in IC engine methane gas, without the hydrogen that burns, ensure internal combustion engine normal operation.
The system and device that internal combustion engine is combined with three Room of electrolysis is made of internal combustion engine and three Room of electrolysis.Because of internal combustion
Machine discharges exhaust gas, needs to be discharged in non-resistance.Therefore, the outlet port of internal combustion engine is connected by pipeline and gas holder
It connects.Gas holder is equipped with air pump, and after the air pressure in gas holder reaches certain pressure, air pump automatic running, air pump is by pipeline gas
Exhaust gas in cabinet is extracted into cover-floating type gas holder.When the air pressure in gas holder reduces zero-pressure, air pump is automatically stopped operation, ensures internal combustion engine
Normal operation.Cover-floating type gas holder acts on：Constant pressure exports exhaust gas.The effect of cooler：Reduce the high-temp waste gas of engine exhaust
Temperature prevents high-temp waste gas from burning methane backeria to death.It is recovery centre of methane backeria poisoning treatment above cooler.Cooler is internal combustion engine
The heat of the high-temp waste gas of discharge is transmitted to recovery centre of methane backeria poisoning treatment, heats in recovery centre of methane backeria poisoning treatment
Sludge water, for methane backeria existence create one go back environment.The outlet port of cover-floating type gas holder and cooler into exhaust outlet
Connection, the outlet port of cooler and being connected into exhaust outlet for the diffluence room of three Room of electrolysis, exhaust gas ascends into methane phase room,
Methane mixed gas is generated, methane mixed gas continues to ascend into separation chamber, and side is set in the methane mixed gas outlet of separation chamber
There is gas block panel.The effect of gas block panel：The sludge water for preventing the methane mixed gas of high-speed cruising from carrying, from methane mixed gas outlet
Discharge reduces the high-speed cruising methane mixed gas speed of service, makes sludge water under the effect of gravity, sinks, and methane mixed gas is because light
And rise, make sludge water and methane mixed gas natural separation.The methane mixed gas outlet of separation chamber and methane mixed gas gas holder
Air inlet connection, the gas discharge outlet of methane mixed gas gas holder be connected to the air inlet of internal combustion engine, internal combustion engine reality
Existing waste gas circulation utilizes zero-emission.
As a kind of preferred embodiment of apparatus of the present invention technical solution, further include organic waste through anaerobic digestion techniques at
Reason, the fermented biogas residue being over are methane strain, and methane strain and the nitrogenous fertilizer matched as required, phosphate fertilizer, water mixing form dirt
Muddy water, sludge water are packed into recovery centre of methane backeria poisoning treatment, the sludge water outlet of recovery centre of methane backeria poisoning treatment
With the sludge water inlet communication of the diffluence room of three Room of electrolysis.Sludge water ascends into methane phase room, and sludge water continues to rise, and enters
Separation chamber sinks because sludge water proportion is more than 1, and methane mixed gas rises naturally because light, sludge water and methane mixed gas shape
At natural separation, sludge water is discharged from the sludge water outlet of separation chamber lower part.Sludge water outlet is equipped with anti-siphonage pipe.Discharge
Mouth is connected to recovery centre of methane backeria poisoning treatment into the sludge mouth of a river, and so far, sludge water realization recycles zero-emission.
Further include the gas discharge outlet of methane mixed gas gas holder as a kind of preferred embodiment of apparatus of the present invention technical solution
It is connected to the air inlet of jet dynamic control.The outlet port of jet dynamic control is connected to cooler into exhaust outlet.Combustion
Gas generating set exports the firewire binding post of alternating current, the input with alternating current inversion of direct current electric equipment (29) respectively of zero curve binding post
Firewire binding post, the connection of zero curve binding post, the positive terminal of the output direct current of alternating current inversion of direct current electric equipment and electrolysis three
The binding post of room anode plate connects.The moon of the negative terminal and three Room of electrolysis of the output direct current of alternating current inversion of direct current electric equipment
The binding post of pole plate connects, and water electrolysis equipment zero consumes commercial energy.
Further include three Room of electrolysis as a kind of preferred embodiment of apparatus of the present invention technical solution, three Room of electrolysis are equipped with production first
Alkane room, anode chamber, cathode chamber and diffluence room and separation chamber.Cathode plate is equipped with permeable hole, and electrolyte membrane is equipped with outside cathode plate.Sun
Pole plate is equipped with permeable hole, and electrolyte membrane is equipped with outside anode plate.Gap is anode chamber between anode plate and anode plate.Cathode plate with
Gap is cathode chamber between cathode plate.Gap is methane phase room between cathode plate and anode plate.Cathode chamber, anode chamber lower part difference
Equipped with water inlet；Top is respectively equipped with water outlet, is equipped with hydrogen discharge at the top of cathode chamber, hydrogen is as merchandise sales.Water inlet
Mouth is connected to the water outlet of water tank, and water outlet is connected to storage pool.Storage pool is equipped with immersible pump, and the water of storage pool passes through diving
Pumping is to water tank.Water tank is equipped with ball-cock assembly, and the water inlet of ball-cock assembly is connected to the water outlet of water electrolysis case.Water electrolysis case into
The mouth of a river is connected to running water pipe.The effect of ball-cock assembly：Cistern water level automatic loading water in a certain range.The work of water electrolysis case
With：Water electrolysis case is equipped with anode plate, cathode plate.Anode plate, cathode plate binding post respectively with alternating current inversion of direct current electric equipment
Anode, negative terminal connection.Water electrolysis case at work, by water electrolysis, removes scale removal, and incrustation scale is prevented to be attached to cathode plate, sun
On pole plate, working efficiency is influenced；Also incrustation scale is prevented to be attached on electrolyte membrane, influences hydrogen ion, oxonium ion passes through.
Operation principle：Electrolysis water is first injected separately into cathode chamber, anode chamber by the first step, into working condition.Second step is opened
DC power supply is opened, keeps anode plate, cathode plate in running order.Third step Pulp pump is recovery centre of methane backeria poisoning treatment
Sludge water namely for methane strain, inject diffluence room, ascend into methane phase room, continue to rise, into separation chamber.Sludge water from point
It is discharged from room outlet, recovery centre of methane backeria poisoning treatment is flowed back into, into working condition.4th step arranges internal combustion engine
The exhaust gas put when the main component of exhaust gas is carbon dioxide or initial start-up, buys bottled carbon dioxide, by exhaust gas from market
Or carbon dioxide injection diffluence room, carbon dioxide rises, into methane phase room.Hydrogen ion that carbon dioxide and water electrolysis generate and
Methane backeria meets.The hydrogen ion that carbon dioxide and water electrolysis generate is under the action of methane backeria, synthesizing methane.At this point, gas at
Point：Methane and carbon dioxide.Gas rises, into separation chamber.Gas is discharged from separation chamber's outlet, into gas holder.Water electrolysis
The hydrogen ion for making anode plate generate forms hydrogen ion water in anode chamber.Hydrogen ion water is under the action of hydraulic pressure, by anode plate
Permeable hole, pass through electrolyte membrane, into methane phase room；Also hydrogen ion cathode plate attraction under, hydrogen ion from anode chamber to
Cathode chamber moves, and passes by methane phase room.Hydrogen ion and carbon dioxide meet, synthesizing methane under the action of methane backeria.It slips through the net
Hydrogen ion enters cathode chamber.In cathode chamber, hydrogen ion is combined with hydrogen ion, generates hydrogen.Hydrogen rises to the top of cathode chamber
Portion, because cathode plate upper end does not have permeable hole, hydrogen to export, collect, as merchandise sales from cathode chamber top delivery outlet.It is cloudy
The oxonium ion that pole plate generates, oxonium ion is under anode plate attraction, into methane phase, continues to move to anode chamber, into anode chamber.
Oxonium ion is combined with oxonium ion, and generates oxygen.Oxygen rises to top in anode chamber, is passed through from the permeable hole on anode plate
It goes, is then passed through electrolyte membrane, into methane phase room top, ascend into separation chamber.It is discharged, enters from separation chamber's gas discharge outlet
Gas holder.At this point, the gas componant in gas holder：The gases such as methane, carbon dioxide, oxygen, are referred to as：Methane mixed gas.Methane is mixed
It is to be transported to internal combustion engine to close gas one.Internal combustion engine realizes that waste gas circulation utilizes zero-emission.Because of the oxygen energy in methane mixed gas
Enough meet the oxygen of combustion in IC engine (acting) demand.Therefore, internal combustion engine burning is done work, and extraneous oxygen ginseng is not needed
With.Also there is no need into air scoop for internal combustion engine.Methane mixed gas second is that being transported to jet dynamic control, send out by generating set
Electricity meets electricity consumption of the present invention.The present invention, which is run, realizes zero consumption commercial energy.
Compared with prior art, the present invention initiates the system and device that internal combustion engine is combined with three Room of electrolysis, makes internal combustion engine
Oxygen in zero consumption commercial energy, zero consumption gas, waste gas circulation utilize zero-emission, exhaust gas no pollution environment.
Description of the drawings
Fig. 1 is present system schematic diagram.
Specific implementation mode
As shown, the system and device that internal combustion engine is combined with three Room of electrolysis, by three Room 2 of internal combustion engine 1 and electrolysis
Composition, which is characterized in that the outlet port 3 of internal combustion engine 1 is connected to cover-floating type gas holder 4 into exhaust outlet 5, cover-floating type gas
The outlet port 6 of cabinet 4 is connected to cooler 7 into exhaust outlet 8, point of the outlet port 9 and three Room 2 of electrolysis of cooler 7
Flow chamber 10 is connected into exhaust outlet 11, and exhaust gas ascends into methane phase room 12, generates methane mixed gas, on methane mixed gas continues
It rises and enters separation chamber 13, side is equipped with gas block panel 15, methane mixed gas discharge in the methane mixed gas outlet 14 of separation chamber 13
Mouth 14 is connected to the air inlet 17 of methane mixed gas gas holder 16, the gas discharge outlet 18 and novel internal combustion of methane mixed gas gas holder 16
The air inlet 19 of machine 1 is connected to, and internal combustion engine realizes that waste gas circulation utilizes zero-emission.
Further include that organic waste is handled through anaerobic digestion techniques, the fermented biogas residue being over is methane strain, methane
Strain and the nitrogenous fertilizer matched as required, phosphate fertilizer, water mixing form sludge water, and sludge water is packed into recovery centre of methane backeria poisoning treatment
In 20, the sludge water of the sludge water outlet 21 of recovery centre of methane backeria poisoning treatment 20 and the diffluence room 10 of three Room 2 of electrolysis into
Mouth 22 is connected to, and sludge water ascends into methane phase room 12, and sludge water continues to rise, into separation chamber 13, because sludge water is than great
Sink in 1, methane mixed gas rises naturally because light, sludge water and methane mixed gas formation natural separation, and sludge water is from separation
The sludge water outlet 23 of 13 lower part of room is discharged, and sludge water outlet 23 is equipped with anti-siphonage pipe 24, outlet 23 in methane backeria
Malicious therapy rehabilitation center 20 is connected into the sludge mouth of a river 25.
Further include that the gas discharge outlet 18 of methane mixed gas gas holder 16 is connected to the air inlet 27 of jet dynamic control 26, combustion
The outlet port 28 of gas generating set 26 is connected to cooler 7 into exhaust outlet 8, and jet dynamic control 26 exports alternating current
Firewire binding post, zero curve binding post connect with the input firewire binding post of alternating current inversion of direct current electric equipment 29, zero curve binding post respectively
It connecing, the positive terminal of the output direct current of alternating current inversion of direct current electric equipment is connect with the binding post of electrolysis three Room, 2 anode plate 30,
The binding post of the negative terminal and the cathode plate 31 of three Room 2 of electrolysis of the output direct current of alternating current inversion of direct current electric equipment 29 connects
It connects.
Further include electrolysis three Room 2, electrolysis three Room 2 be equipped with methane phase room 12, anode chamber 32, cathode chamber 33 and diffluence room 10 and
Separation chamber 13, cathode plate 31 are equipped with permeable hole 34, and 31 outside of cathode plate is equipped with electrolyte membrane 35, and anode plate 30 is equipped with permeable hole
34, the outside of anode plate 30 is equipped with electrolyte membrane 35, and gap is anode chamber 32 between anode plate 30 and anode plate 30, cathode plate 31 with
Gap is cathode chamber 33 between cathode plate 31, and gap is methane phase room 12, cathode chamber 33, sun between cathode plate 31 and anode plate 30
32 lower part of pole room is respectively equipped with water inlet 36, and top is respectively equipped with water outlet 37, and 33 top of cathode chamber is equipped with hydrogen discharge 38,
Hydrogen is connected to as merchandise sales, water inlet 36 with the water outlet of water tank 39, and water outlet 37 is connected to storage pool 40, storage pool
40 are equipped with immersible pump 41, and storage pool 40 is extracted into water tank 39 by immersible pump 41, and water tank 39 is equipped with ball-cock assembly 42, ball-cock assembly 42
Water inlet is connected to the water outlet of water electrolysis case 43, and the water inlet of water electrolysis case 43 is connected to running water pipe 44.
Those skilled in the art design mounting technique according to description of the invention and Figure of description and specific embodiment
Scheme carries out the link between installation and each equipment, debugging, trial operation, operation from market purchase of equipment or home-built equipment.
Claims (4)
1. the system and device that internal combustion engine is combined with three Room of electrolysis, is made of internal combustion engine (1) and electrolysis three rooms (2),
It is characterized in that, the outlet port (3) of internal combustion engine (1) is connected to cover-floating type gas holder (4) into exhaust outlet (5), cover-floating type
The outlet port (6) of gas holder (4) is connected to cooler (7) into exhaust outlet (8), the outlet port (9) of cooler (7) with
It is electrolysed being connected into exhaust outlet (11) for the diffluence room (10) of three rooms (2), exhaust gas ascends into methane phase room (12), and it is mixed to generate methane
Gas is closed, methane mixed gas continues to ascend into separation chamber (13), methane mixed gas outlet (14) the interior side of separation chamber (13)
Equipped with gas block panel (15), methane mixed gas outlet (14) is connected to the air inlet (17) of methane mixed gas gas holder (16), methane
The gas discharge outlet (18) of gaseous mixture gas holder (16) is connected to the air inlet (19) of internal combustion engine (1), and internal combustion engine is realized
Waste gas circulation utilizes zero-emission.
2. the system and device that internal combustion engine according to claim 1 is combined with three Room of electrolysis, which is characterized in that further include
Organic waste is handled through anaerobic digestion techniques, the fermented biogas residue being over be methane strain, methane strain with match as required
The nitrogenous fertilizer of ratio, phosphate fertilizer, water mixing form sludge water, and sludge water is packed into methane backeria recovery centre of poisoning treatment (20), methane backeria
The sludge water inlet of the sludge water outlet (21) of recovery centre of poisoning treatment (20) and the diffluence room (10) of electrolysis three rooms (2)
(22) it is connected to, sludge water ascends into methane phase room (12), and sludge water continues to rise, into separation chamber (13), because of sludge water ratio
Great to sink in 1, methane mixed gas rises naturally because light, sludge water and methane mixed gas formation natural separation, sludge water from
The sludge water outlet (23) of separation chamber (13) lower part is discharged, and sludge water outlet (23) is equipped with anti-siphonage pipe (24), outlet
(23) it is connected into the sludge mouth of a river (25) with recovery centre of methane backeria poisoning treatment (20), so far, sludge water circulation use zero-emission
It puts.
3. the system and device that internal combustion engine according to claim 1 is combined with three Room of electrolysis, which is characterized in that further include
The gas discharge outlet (18) of methane mixed gas gas holder (16) is connected to the air inlet (27) of jet dynamic control (26), fuel gas generation
The outlet port (28) of unit (26) is connected to cooler (7) into exhaust outlet (8), jet dynamic control (26) output exchange
Input firewire binding post, zero curve of the firewire binding post, zero curve binding post of electricity respectively with alternating current inversion of direct current electric equipment (29) connect
Terminal connects, the positive terminal and electrolysis three rooms (2) anode plate (30) of the output direct current of alternating current inversion of direct current electric equipment
Binding post connects, the cathode of the negative terminal and electrolysis three rooms (2) of the output direct current of alternating current inversion of direct current electric equipment (29)
The binding post of plate (31) connects, and water electrolysis equipment realizes zero consumption commercial energy.
4. the system and device that internal combustion engine according to claim 1 is combined with three Room of electrolysis, which is characterized in that further include
Three rooms (2) are electrolysed, electrolysis three rooms (2) is equipped with methane phase room (12), anode chamber (32), cathode chamber (33) and diffluence room (10) and divides
From room (13), cathode plate (31) is equipped with permeable hole (34), is equipped with electrolyte membrane (35) outside cathode plate (31), anode plate (30) is set
There is permeable hole (34), is equipped with electrolyte membrane (35) outside anode plate (30), gap is between anode plate (30) and anode plate (30)
Anode chamber (32), gap is cathode chamber (33), cathode plate (31) and anode plate (30) between cathode plate (31) and cathode plate (31)
Between gap be methane phase room (12), cathode chamber (33), anode chamber (32) lower part be respectively equipped with water inlet (36), and top is set respectively
There is water outlet (37), is equipped with hydrogen discharge (38) at the top of cathode chamber (33), hydrogen is as merchandise sales, water inlet (36) and water
The water outlet of case (39) is connected to, and water outlet (37) is connected to storage pool (40), and storage pool (40) is equipped with immersible pump (41), storage
Pond (40) is extracted into water tank (39) by immersible pump (41), and water tank (39) is equipped with ball-cock assembly (42), the water inlet of ball-cock assembly (42)
It is connected to the water outlet of water electrolysis case (43), the water inlet of water electrolysis case (43) is connected to running water pipe (44).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810473433.7A CN108468063A (en) | 2018-05-09 | 2018-05-09 | The system and device that internal combustion engine is combined with three Room of electrolysis |
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| CN201810473433.7A CN108468063A (en) | 2018-05-09 | 2018-05-09 | The system and device that internal combustion engine is combined with three Room of electrolysis |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004192824A (en) * | 2002-12-06 | 2004-07-08 | Chubu Electric Power Co Inc | Fuel cell/methane fermentation cycle system |
| CN104176823A (en) * | 2014-07-09 | 2014-12-03 | 浙江大学 | Microbial electrolytic system and method integrating biological treatment of wastewater and promotion of methane recovery |
| 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 |
| CN207175939U (en) * | 2017-06-28 | 2018-04-03 | 高节义 | It is electrolysed three Room and produces the setting of methane system |
-
2018
- 2018-05-09 CN CN201810473433.7A patent/CN108468063A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004192824A (en) * | 2002-12-06 | 2004-07-08 | Chubu Electric Power Co Inc | Fuel cell/methane fermentation cycle system |
| CN104176823A (en) * | 2014-07-09 | 2014-12-03 | 浙江大学 | Microbial electrolytic system and method integrating biological treatment of wastewater and promotion of methane recovery |
| 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 |
| CN207175939U (en) * | 2017-06-28 | 2018-04-03 | 高节义 | It is electrolysed three Room and produces the setting of methane system |
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Application publication date: 20180831 |