CN109140523A - Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation - Google Patents

Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation Download PDF

Info

Publication number
CN109140523A
CN109140523A CN201710554157.2A CN201710554157A CN109140523A CN 109140523 A CN109140523 A CN 109140523A CN 201710554157 A CN201710554157 A CN 201710554157A CN 109140523 A CN109140523 A CN 109140523A
Authority
CN
China
Prior art keywords
stove
pot
outlet
electrolysis
methane
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
Application number
CN201710554157.2A
Other languages
Chinese (zh)
Inventor
高节义
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN201710554157.2A priority Critical patent/CN109140523A/en
Publication of CN109140523A publication Critical patent/CN109140523A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24CDOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
    • F24C3/00Stoves or ranges for gaseous fuels
    • F24C3/008Ranges
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12MAPPARATUS 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
    • C12M21/00Bioreactors or fermenters specially adapted for specific uses
    • C12M21/04Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24CDOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
    • F24C13/00Stoves or ranges with additional provisions for heating water

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Genetics & Genomics (AREA)
  • Mechanical Engineering (AREA)
  • Organic Chemistry (AREA)
  • Molecular Biology (AREA)
  • Zoology (AREA)
  • Combustion & Propulsion (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Wood Science & Technology (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Sustainable Development (AREA)
  • Biomedical Technology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Biochemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation, it is made of stove (1) and pot (2) and electrolysis three rooms (3) and hydraulic type biomass pool (4), it is characterized in that, the gas discharge outlet (5) for being electrolysed three rooms (3) is connected to the switch (6) of stove (1), switch (6) is connected to the tray for combustion (7) in burner hearth, tray for combustion (7) is located at the lower part of the chamber of a kitchen range, tray for combustion (7) is equipped with ignition (8), refractory seals pad (9) are equipped between stove (1) and pot suitable for reading (2), stove (1) internal upper part is equipped with outlet port (10), the pipeline periphery of outlet port (10) is equipped with sealing type cistern (11), sealing type cistern (11) top is additionally provided with hot water discharge pipe, hot water discharge pipe mouthful is equipped with tap (15), the discharge of pot and stove exhaust gas Mouth (10) is connected to the air inlet (16) of electrolysis three rooms (3).

Description

Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation
Technical field
The present invention relates to a kind of family cooking pot and stove energy, oxygen self-sufficiency, waste gas circulation utilizes the device of zero-emission.
Background technique
It is well known that pot and stove is cooked, need to burn conventional energy resource, also discharge exhaust gas, pollute environment.Pot and stove must also be equipped with Into air scoop, comburant oxygen, conventional energy resource, which could burn, cooks.Therefore, a kind of power self-support is studied, waste gas circulation utilizes zero-emission The pot and stove put is the current technical issues that need to address.
Summary of the invention
The technical problems to be solved by the present invention are: family pot and stove energy oxygen self-sufficiency waste gas circulation setting using zero-emission It sets.
The present invention the technical solution to solve the technical problem is that:
Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation, by stove and pot and three Room of electrolysis and water Methane tank composition.The gas discharge outlet for being electrolysed three Room is connected to the switch of stove, and switch is connected to the tray for combustion in burner hearth, Tray for combustion is located at the lower part of the chamber of a kitchen range.Tray for combustion effect: homogenous combustion.Tray for combustion is equipped with ignition, stove and pot suitable for reading it Between be equipped with refractory seals pad, the effect of refractory seals pad: first is that the chamber of a kitchen range and air exclusion;Second is that explosion-proof.Stove internal upper part Equipped with outlet port, the pipeline periphery of outlet port is equipped with sealing type cistern, and the high-temp waste gas for discharging pot and stove heats water Water in case.Sealing type cistern is equipped with air vent.The effect of air vent: in toward water tank plus when water, air is discharged.Water tank discharges water When, suck.The top of sealing type cistern is equipped with ball valve, and the water inlet pipe of ball valve is connected to running water pipe.The effect of ball valve: automatic Upper water makes cistern water level control within the scope of certain.Enclosed water upper box part is additionally provided with hot water discharge pipe, hot water discharge pipe Mouth is equipped with tap.The effect of tap: for hot water for life.Pot and stove outlet port is connected to the air inlet of three Room of electrolysis. It is electrolysed the methane mixed gas of three Room generation, methane mixed gas rises, the gas discharge outlet discharge from three Room of electrolysis, gas discharge outlet It is connected to the switch of stove.
As a kind of preferred embodiment of apparatus of the present invention technical solution, further include three Room of electrolysis by methane phase room, cathode chamber, Anode chamber's composition.Methane phase room, cathode chamber, anode chamber are respectively equipped with gas discharge outlet at top.Methane phase room top is additionally provided with Sludge water outlet, sludge water outlet are connected to hydraulic type biomass pool.The bottom of hydraulic type biomass pool is equipped with into nutrient solution mouth, It is connected into nutrient solution mouth with nutrition liquid pool.The bottom of hydraulic type biomass pool is additionally provided with sludge water outlet, sludge water outlet with It is located at the sludge water inlet communication of methane phase room bottom.Be equipped with biogas delivery outlet at the top of hydraulic type biomass pool, biogas delivery outlet with The air inlet of the switch of stove is connected to.
Working principle;1, three Room of the electrolysis method of producing methane, comprises the following steps that: 1. first will originally water electrolysis, Or when because of sludge dilutional hyponatremia in hydraulic type biomass pool, the supernatant of extra sludge water is extracted into filter, filtered water, It is being electrolysed.Electrolysis water is stored in storage pool, and the electrolysis water in storage pool is automatically injected water tank by water pump.Setting in water tank Ball valve, ball valve make water level be maintained at certain range.Water tank is connected to cathode chamber, anode chamber respectively.The position of water tank is higher than sun The position of pole room, cathode chamber forms certain hydraulic pressure between water tank and anode chamber, cathode chamber, enable electrolysis water from cathode chamber, Anode chamber flows rapidly to methane phase room by electrolyte membrane (screen cloth) automatically.2. again by nitrogenous fertilizer, phosphate fertilizer, a small amount of other elements and Electrolysis water is packed into nutrition liquid pool, mixes, and 3. fills methane strain (under anaerobic environment, organic matter fermentation is over for methane strain) Enter hydraulic type biomass pool, the nutrient solution in nutrition liquid pool is extracted into hydraulic type biomass pool, nutrient solution and methane strain with sewage pump It stirs evenly, forms sludge water, the sludge water (methane strain) in hydraulic type biomass pool is extracted into methane phase room bottom with sewage pump, from The discharge of methane phase room upper nozzle, overflows to methane-generating pit, sludge water (methane strain) recycles.
2, further include the exhaust gas of boiler engine exhaust, exhaust gas is transported to by air pump by deduster, in heating methane tank Sludge water, improve methane tank gas production rate, the waste gas outlet of deduster is connected to the bottom air inlet of methane phase room, and exhaust gas passes through Gas distribution plate rises rapidly evenly into methane phase room, at this point, water electrolyzer start to work, anode plate generate hydrogen from Son forms hydrogen ion water in anode chamber, 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, Hydrogen ion water flows to methane phase room in the presence of hydraulic pressure, by asymmetric diaphragm automatically.Second is that hydrogen ion water is inhaled in cathode plate Under drawing, through asymmetric electrolyte membrane into cathode plate transfer process, when passing by methane phase room, the hydrogen ion in hydrogen ion water exists Methane phase room is met with the methane backeria in the carbon dioxide and sludge water in exhaust gas, the work of carbon dioxide and hydrogen ion in methane backeria Under, synthesizing methane.Meanwhile also discharging oxygen.Methane gas and oxygen rise, and export from gas delivery port, are transported to boiler In internal combustion engine, methane does work (burning), and oxygen participates in methane acting (combustion-supporting), and waste gas circulation utilizes zero-emission.The hydrogen slipped through the net from Son enters cathode chamber, and hydrogen ion generates hydrogen in conjunction with hydrogen ion, and hydrogen rises, and by upper gas delivery outlet, is transported to pot Furnace internal combustion engine does work (burning), and waste gas circulation utilizes zero-emission.The oxonium ion that cathode plate generates is shifted to anode plate, in anode chamber Oxonium ion is combined with oxonium ion generation oxygen, and oxygen rises, and exports from oxygen delivery outlet, is transported to boiler internal combustion engine, participates in first Alkane, hydrogen acting (combustion-supporting) realize that waste gas circulation utilizes zero-emission.
It 3, further include in methane phase room, methane backeria encounters oxonium ion, oxygen, and oxonium ion, oxygen poison methane backeria, part It after methane backeria poisoning, rises rapidly, is discharged from sludge water outlet, overflows to methane-generating pit, the methane backeria of poisoning is in methane-generating pit The oxonium ion of carrying, oxygen and rehabilitation of recuperating are eaten up by aerobic bacteria, therefore, the volume of the volume of methane-generating pit than methane phase room Greatly.
It 4, further include the exhaust gas of boiler engine exhaust, the hydrogen ion generated in methane phase room with water electrolysis meets, Under the action of methane backeria, synthesizing methane, meanwhile, oxygen is also discharged, the hydrogen that the oxygen and cathode chamber generated there are also anode chamber generates Gas, methane, hydrogen are transported to boiler internal combustion engine acting (burning), and oxygen participates in methane, hydrogen acting (combustion-supporting), generates titanium dioxide Carbon and water form the anaerobic digestion resource circulation utilization period, and each element is recycled in closed container, do not lost, therefore, Boiler internal combustion engine can be realized the energy, oxygen self-sufficiency, and waste gas circulation utilizes zero-emission.
Compared with prior art, the present invention can be realized the family pot and stove energy, oxygen self-sufficiency waste gas circulation utilizes zero-emission.
Detailed description of the invention
Fig. 1 is system schematic of the invention.
Specific embodiment
As shown, family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation, by 2 He of stove 1 and pot It is electrolysed three Room 3 and hydraulic type biomass pool 4 forms, which is characterized in that the gas discharge outlet 5 of three Room 3 of electrolysis and the switch 6 of stove 1 Connection, switch 6 are connected to the tray for combustion 7 in burner hearth, and tray for combustion 7 is located at the lower part of the chamber of a kitchen range, and tray for combustion 7 is equipped with ignition 8, Refractory seals pad 9 is equipped between stove 1 and pot suitable for reading 2,1 internal upper part of stove is equipped with outlet port 10, outlet port 10 Pipeline periphery be equipped with sealing type cistern 11, sealing type cistern 11 is equipped with air vent 12, and the top of sealing type cistern 11 is equipped with ball The water inlet pipe of valve 13, ball valve 13 is connected to running water pipe 14, and 11 top of sealing type cistern is additionally provided with hot water discharge pipe, hot water discharge Nozzle is equipped with tap 15, and pot and stove outlet port 10 is connected to the air inlet 16 of three Room 3 of electrolysis, the first that three Room 3 of electrolysis generate Alkane gaseous mixture, methane mixed gas rise, and are discharged from the gas discharge outlet 5 of three Room 3 of electrolysis, the switch of gas discharge outlet 5 and stove 1 6 connections.
It further include that three Room 3 of electrolysis are made of methane phase room 17, cathode chamber 18, anode chamber 19, methane phase room 17, cathode chamber 18, anode chamber 19 is respectively equipped with gas discharge outlet 5 at top, and 17 top of methane phase room is additionally provided with sludge water outlet 20, sludge Water outlet 20 is connected to hydraulic type biomass pool 4, and the bottom of hydraulic type biomass pool 4 is equipped with into nutrient solution mouth 21, into nutrient solution mouth 21 are connected to nutrition liquid pool 22, and the bottom of hydraulic type biomass pool 4 is additionally provided with sludge water outlet 23, sludge water outlet 23 with set Sludge water inlet 24 in 17 bottom of methane phase room is connected to, and biogas delivery outlet 25, biogas output are equipped at the top of hydraulic type biomass pool 4 Mouth 25 is connected to the air inlet of the switch 6 of stove 1.

Claims (2)

1. family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation, by stove (1) and pot (2) and three Room of electrolysis (3) and hydraulic type biomass pool (4) forms, which is characterized in that the gas discharge outlet (5) of electrolysis three rooms (3) and the switch of stove (1) (6) it is connected to, switch (6) is connected to the tray for combustion (7) in burner hearth, and tray for combustion (7) is located at the lower part of the chamber of a kitchen range, and tray for combustion (7) is equipped with Ignition (8) is equipped with refractory seals pad (9) between stove (1) and pot suitable for reading (2), and stove (1) internal upper part is equipped with exhaust gas The pipeline periphery of outlet (10), outlet port (10) is equipped with sealing type cistern (11), and sealing type cistern (11), which is equipped with, deflates The top in hole (12), sealing type cistern (11) is equipped with ball valve (13), and the water inlet pipe of ball valve (13) is connected to running water pipe (14), seals Closed type water tank (11) top is additionally provided with hot water discharge pipe, and hot water discharge pipe mouthful is equipped with tap (15), pot and stove outlet port (10) it being connected to the air inlet (16) of electrolysis three rooms (3), the methane mixed gas that electrolysis three rooms (3) generates, methane mixed gas rises, From gas discharge outlet (5) discharge of electrolysis three rooms (3), gas discharge outlet (5) is connected to the switch (6) of stove (1).
2. family according to claim 1 utilizes the setting of zero-emission, feature with pot and stove energy oxygen self-sufficiency waste gas circulation It is, further includes that electrolysis three rooms (3) is made of methane phase room (17), cathode chamber (18), anode chamber (19), methane phase room (17), Cathode chamber (18), anode chamber (19) are respectively equipped with gas discharge outlet (5) at top, and methane phase room (17) top is additionally provided with sludge water Outlet (20), sludge water outlet (20) are connected to hydraulic type biomass pool (4), the bottom of hydraulic type biomass pool (4) be equipped with into Nutrient solution mouth (21) is connected into nutrient solution mouth (21) with nutrition liquid pool (22), and the bottom of hydraulic type biomass pool (4) is additionally provided with sludge Water outlet (23), sludge water outlet (23) are connected to the sludge water inlet (24) for being located at methane phase room (17) bottom, hydraulic pressure Biogas delivery outlet (25) are equipped at the top of formula methane-generating pit (4), the air inlet of the switch (6) of biogas delivery outlet (25) and stove (1) connects It is logical.
CN201710554157.2A 2017-06-28 2017-06-28 Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation Pending CN109140523A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710554157.2A CN109140523A (en) 2017-06-28 2017-06-28 Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710554157.2A CN109140523A (en) 2017-06-28 2017-06-28 Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation

Publications (1)

Publication Number Publication Date
CN109140523A true CN109140523A (en) 2019-01-04

Family

ID=64803234

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710554157.2A Pending CN109140523A (en) 2017-06-28 2017-06-28 Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation

Country Status (1)

Country Link
CN (1) CN109140523A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201954596U (en) * 2010-11-26 2011-08-31 朱武 Oil and gas dual-purpose full-automatic civil kitchen range
CN205560872U (en) * 2016-04-21 2016-09-07 永康市华港厨具配件有限公司 Power adjustable intelligence commercial fuel gas stove
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

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201954596U (en) * 2010-11-26 2011-08-31 朱武 Oil and gas dual-purpose full-automatic civil kitchen range
CN205560872U (en) * 2016-04-21 2016-09-07 永康市华港厨具配件有限公司 Power adjustable intelligence commercial fuel gas stove
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

Similar Documents

Publication Publication Date Title
CN101560466B (en) Integrated methane dry fermentation device
CN204162707U (en) A kind of unpowered from stirring broken shell anaerobic ferment devices
CN106835186A (en) It is electrolysed the method and device that methane is produced in three Room
CN101724551B (en) Full mixed anaerobic reaction circulating device and circulating method for methane reaction raw materials
CN110468045A (en) A kind of preaeration heating batch-type anaerobic dry fermentation apparatus and method
CN2825645Y (en) Combined tank type marsh gas and marsh liquid generator
CN206706104U (en) A kind of solar-energy methane pit
CN105567561A (en) Underground-type two-stage anaerobic large-medium biogas digester achieving automatic high temperature fermentation
CN206929758U (en) Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission
CN207741146U (en) Family cooking pot and stove
CN207729841U (en) Family heating small boiler
CN208414409U (en) Novel normal-pressure boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission
CN207175939U (en) It is electrolysed three Room and produces the setting of methane system
CN109136070A (en) Family utilizes the setting of zero-emission with heating system energy oxygen self-sufficiency waste gas circulation
CN109140523A (en) Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation
CN201981201U (en) Solid organism high-efficiency biogas fermentation system
CN109136072A (en) Novel normal-pressure boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission
CN205368382U (en) Novel marsh gas tank
CN207016766U (en) A kind of diphasic anaerobic fermentation system stirred using dynamic hydraulic combined
CN109140465A (en) Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission
CN207581801U (en) A kind of mixed material fermentation and biogas production device with low temperature sterilization
CN105624203A (en) Method for producing biogas from cassava alcohol waste liquid as raw material
CN206447878U (en) A kind of biomass marsh gas TRT
CN201427968Y (en) Top and bottom internal recycle biomass pool
CN218290895U (en) Novel biogas slurry and biogas water-fertilizer integrated machine

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20190104

RJ01 Rejection of invention patent application after publication