CN109140465A - Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission - Google Patents
Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission Download PDFInfo
- Publication number
- CN109140465A CN109140465A CN201710554159.1A CN201710554159A CN109140465A CN 109140465 A CN109140465 A CN 109140465A CN 201710554159 A CN201710554159 A CN 201710554159A CN 109140465 A CN109140465 A CN 109140465A
- Authority
- CN
- China
- Prior art keywords
- water
- novel steam
- steam boiler
- waste gas
- air inlet
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
-
- 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
Landscapes
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Genetics & Genomics (AREA)
- General Engineering & Computer Science (AREA)
- Sustainable Development (AREA)
- Biomedical Technology (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Molecular Biology (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mechanical Engineering (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission, it is made of Novel steam gas boiler (1) and electrolysis three rooms (2), it is characterized in that, the air inlet (3) of novel steam boiler (1) is connected to the gas discharge outlet (4) of electrolysis three rooms (2), air inlet (3) is connected to biogas spray head (5), each biogas spray head (5) is equipped with ignition (6), the circumferential periphery of the burner hearth of novel steam boiler (1) is equipped with water tank (7), the water inlet of water tank (7) bottom is connected to the water outlet of high-pressure hydraulic pump (12), the water inlet of high-pressure hydraulic pump (12) is connected to running water pipe (13), the roof of the furnace of novel steam boiler (1) is equipped with multiple high-temp waste gas discharge pipes (14), the air inlet of high-temp waste gas discharge pipe (14) and methane phase room (16) (15) it is connected to.
Description
Technical field
The present invention relates to the settings that a kind of novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes zero-emission.
Background technique
It is well known that steam boiler, need to burn conventional energy resource, also discharge exhaust gas, pollute environment.Steam boiler one will be set
There is stockhole；Two will be equipped with into air scoop, comburant oxygen.Therefore, it is self-supporting that a kind of novel steam boiler energy, oxygen are studied, is given up
Gas recycles the setting of zero-emission, is the current technical issues that need to address.
Summary of the invention
The technical problem to be solved by the present invention is to novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes zero-emission
Setting.
The present invention the technical solution to solve the technical problem is that:
Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission.Because of steam copper currently on the market
Furnace is designed with fire grate, clinker storage room, stockhole.And the burner hearth of steam boiler of the present invention be it is closed, both without fire grate, do not have yet
Have that clinker storage room, there are no stockholes, also not into air scoop, therefore claims novel steam boiler.Novel steam boiler energy oxygen
Gas self-sufficiency waste gas circulation utilizes the setting of zero-emission, is made of Novel steam gas boiler and three Room of electrolysis.Novel steam boiler
Air inlet is connected to the gas discharge outlet of three Room of electrolysis.Air inlet is connected to the air inlet for being located at biogas spray head in burner hearth.In furnace
Lower part is equipped with multiple biogas spray heads in thorax, and each biogas spray head is equipped with ignition.The surrounding of the burner hearth of novel steam boiler
Periphery is equipped with water tank, and water tank is additionally provided with water-level gauge, air gauge, vapor outlet.Water tank periphery is equipped with insulating layer.In burner hearth
Top is equipped with multiple S type heat-exchange tubes, and the suitable for reading and lower mouth of multiple S heat-exchange tubes is connected to water tank respectively.Water tank bottom into
The mouth of a river is connected to the water outlet of high-pressure hydraulic pump, and the water inlet of high-pressure hydraulic pump is connected to running water pipe.The burner hearth of novel steam boiler
Top is equipped with multiple high-temp waste gas discharge pipes and is merged into a pipe, nozzle after multiple high-temp waste gas discharge pipes pass through water tank (7)
It is connected to the air inlet of the methane phase room of three Room of electrolysis.
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 novel normal-pressure boiler is connected to.
Working principle: 1, be electrolysed the three Room method of producing methane, comprise 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 automatically.2. again by nitrogenous fertilizer, phosphate fertilizer, a small amount of other elements and electrolysis water
It is packed into nutrition liquid pool, is mixed, methane strain (under anaerobic environment, organic matter fermentation is over for methane strain) is 3. packed into hydraulic pressure
Nutrient solution in nutrition liquid pool is extracted into hydraulic type biomass pool with sewage pump by formula methane-generating pit, and nutrient solution is stirred evenly with methane strain, shape
At sludge water, the sludge water (methane strain) in hydraulic type biomass pool is extracted into methane phase room bottom with sewage pump, from methane phase
The discharge of 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 release oxygen, methane gas and oxygen rise, export from gas delivery port, be transported to boiler
In internal combustion engine, methane does work (burning), and oxygen participates in methane acting (combustion-supporting), waste gas circulation using 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 one does not consume conventional energy resource；Two not oxygen in consumed cabin air；Three to air
Middle discharge exhaust gas, can be realized the energy, oxygen self-sufficiency, and waste gas circulation utilizes zero-emission；
Detailed description of the invention
Fig. 1 is system schematic of the invention；
Specific embodiment
As shown, novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission, by Novel steam
Gas boiler 1 and three Room 2 of electrolysis composition.The air inlet 3 of novel steam boiler 1 is connected to the gas discharge outlet 4 of three Room 2 of electrolysis, into
Port 3 is connected to the air inlet for being located at biogas spray head 5 in burner hearth, and lower part is equipped with multiple biogas spray heads 5, each biogas in burner hearth
Spray head 5 is equipped with ignition 6, and the circumferential periphery of the burner hearth of novel steam boiler 1 is equipped with water tank 7, and water tank 7 is additionally provided with water-level gauge
8, air gauge 9, vapor outlet 10, the top in burner hearth are equipped with multiple S type heat-exchange tubes 11, multiple S heat-exchange tubes 11
Suitable for reading and lower mouth is connected to water tank (7) respectively, and the water inlet of water tank (7) bottom is connected to the water outlet of high-pressure hydraulic pump (12), high
The water inlet of water pump 12 is connected to running water pipe 13, and the roof of the furnace of novel steam boiler 1 is discharged equipped with multiple high-temp waste gas
It manages (14), after multiple high-temp waste gas discharge pipes 14 pass through water tank 7, is merged into a pipe, the methane phase room of three Room 2 of nozzle and electrolysis
16 air inlet 15 is connected to.
It further include that three Room 2 of electrolysis are made of methane phase room 16, cathode chamber 17, anode chamber 18, methane phase room 16, cathode chamber
17, anode chamber 18 is respectively equipped with gas discharge outlet 4 at top, and 16 top of methane phase room is additionally provided with sludge water outlet 19, sludge
Water outlet 19 is connected to hydraulic type biomass pool 20, and the bottom of hydraulic type biomass pool 20 is equipped with into nutrient solution mouth 21, into nutrient solution
Mouth 21 is connected to nutrition liquid pool 22, and the bottom of hydraulic type biomass pool 20 is additionally provided with sludge water outlet 23, sludge water outlet 23
It is connected to the sludge water inlet 24 for being located at 16 bottom of methane phase room, biogas delivery outlet 25, natural pond is equipped at the top of hydraulic type biomass pool 20
Gas delivery outlet 25 is connected to the air inlet 3 of novel normal-pressure boiler 1.
Claims (2)
1. novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission, by Novel steam gas boiler (1) and
It is electrolysed three rooms (2) composition, which is characterized in that the air inlet (3) of novel steam boiler (1) and the gas of electrolysis three rooms (2) are discharged
Mouth (4) connection, air inlet (3) are connected to the air inlet for being located at biogas spray head (5) in burner hearth, and lower part is equipped with multiple natural ponds in burner hearth
Gas nozzle (5), each biogas spray head (5) are equipped with ignition (6), and the circumferential periphery of the burner hearth of novel steam boiler (1) is set
Have water tank (7), water tank (7) is additionally provided with water-level gauge (8), air gauge (9), vapor outlet (10), and the top in burner hearth is equipped with
The suitable for reading and lower mouth of multiple S type heat-exchange tubes (11), multiple S heat-exchange tubes (11) is connected to water tank (7) respectively, water tank (7) bottom
The water inlet in portion is connected to the water outlet of high-pressure hydraulic pump (12), and the water inlet of high-pressure hydraulic pump (12) is connected to running water pipe (13),
The roof of the furnace of novel steam boiler (1) is equipped with multiple high-temp waste gas discharge pipes (14), and multiple high-temp waste gas discharge pipes (14) are worn
After crossing water tank (7), it is merged into a pipe, nozzle is connected to the air inlet (15) of the methane phase room (16) of electrolysis three rooms (2).
2. novel steam boiler energy oxygen self-sufficiency waste gas circulation according to claim 1 utilizes the setting of zero-emission,
It is characterized in that, further includes that electrolysis three rooms (2) is made of methane phase room (16), cathode chamber (17), anode chamber (18), methane phase room
(16), cathode chamber (17), anode chamber (18) are respectively equipped with gas discharge outlet (4) at top, and methane phase room (16) top is additionally provided with
Sludge water outlet (19), sludge water outlet (19) are connected to hydraulic type biomass pool (20), the bottom of hydraulic type biomass pool (20)
Portion is equipped with into nutrient solution mouth (21), is connected into nutrient solution mouth (21) with nutrition liquid pool (22), the bottom of hydraulic type biomass pool (20)
It is additionally provided with sludge water outlet (23), sludge water outlet (23) and the sludge water inlet (24) for being located at methane phase room (16) bottom
Connection, hydraulic type biomass pool (20) top are equipped with biogas delivery outlet (25), biogas delivery outlet (25) and novel normal-pressure boiler (1)
Air inlet (3) connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710554159.1A CN109140465A (en) | 2017-06-28 | 2017-06-28 | Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710554159.1A CN109140465A (en) | 2017-06-28 | 2017-06-28 | Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109140465A true CN109140465A (en) | 2019-01-04 |
Family
ID=64803157
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710554159.1A Pending CN109140465A (en) | 2017-06-28 | 2017-06-28 | Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109140465A (en) |
Citations (5)
| 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 |
| WO2012156588A1 (en) * | 2011-05-18 | 2012-11-22 | Fortum Oyj | A method and an apparatus for producing energy by recycling materials during a fuel combustion process |
| CN105783243A (en) * | 2016-05-19 | 2016-07-20 | 佛山市晟恺热能设备有限公司 | Instant household gas steam boiler and pipeline system thereof |
| CN205619364U (en) * | 2016-04-25 | 2016-10-05 | 代成璐 | High -efficient marsh gas generation burner of environmental protection |
| 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 |
-
2017
- 2017-06-28 CN CN201710554159.1A patent/CN109140465A/en active Pending
Patent Citations (5)
| 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 |
| WO2012156588A1 (en) * | 2011-05-18 | 2012-11-22 | Fortum Oyj | A method and an apparatus for producing energy by recycling materials during a fuel combustion process |
| CN205619364U (en) * | 2016-04-25 | 2016-10-05 | 代成璐 | High -efficient marsh gas generation burner of environmental protection |
| CN105783243A (en) * | 2016-05-19 | 2016-07-20 | 佛山市晟恺热能设备有限公司 | Instant household gas steam boiler and pipeline system 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 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106835186A (en) | It is electrolysed the method and device that methane is produced in three Room | |
| CN204162707U (en) | A kind of unpowered from stirring broken shell anaerobic ferment devices | |
| CN102586334A (en) | Method for producing biogas from kitchen wastes by anaerobic fermentation | |
| CN108658361A (en) | The integrated livestock and poultry cultivating system of biomass cogeneration of heat and power | |
| CN2825645Y (en) | Combined tank type marsh gas and marsh liquid generator | |
| CN103708693A (en) | Digestion system and method for sludge produced by urban sewage treatment | |
| CN102617006A (en) | Biogas power generation system | |
| CN204607785U (en) | Novel energy-conserving effluent treatment plant | |
| CN208414409U (en) | Novel normal-pressure boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission | |
| CN206929758U (en) | Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission | |
| CN109136072A (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 | |
| CN201981201U (en) | Solid organism high-efficiency biogas fermentation system | |
| CN207729841U (en) | Family heating small boiler | |
| CN109140465A (en) | Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission | |
| CN109136070A (en) | Family utilizes the setting of zero-emission with heating system energy oxygen self-sufficiency waste gas circulation | |
| CN102586095B (en) | Gas stripping convective circulation anaerobic digestion reactor | |
| CN207741146U (en) | Family cooking pot and stove | |
| CN203976787U (en) | A kind of fecal sewage treatment methane-generating pit | |
| CN203904067U (en) | Efficient anaerobic reactor for secondary anaerobic treatment of fuel ethanol wastewater | |
| CN209636221U (en) | Type of providing multiple forms of energy to complement each other marsh gas fermenting system | |
| CN109140523A (en) | Family utilizes the setting of zero-emission with pot and stove energy oxygen self-sufficiency waste gas circulation | |
| CN206645976U (en) | The integrated livestock and poultry cultivating system of biomass cogeneration of heat and power | |
| CN105624203A (en) | Method for producing biogas from cassava alcohol waste liquid as raw material | |
| CN108753845A (en) | The method of carbon dioxide preparation methane and its setting |
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 | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190104 |