CN206929758U - 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
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- CN206929758U CN206929758U CN201720830941.7U CN201720830941U CN206929758U CN 206929758 U CN206929758 U CN 206929758U CN 201720830941 U CN201720830941 U CN 201720830941U CN 206929758 U CN206929758 U CN 206929758U
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- Prior art keywords
- novel steam
- waste gas
- steam boiler
- water
- connects
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- 239000002912 waste gas Substances 0.000 title claims abstract description 31
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 27
- 239000001301 oxygen Substances 0.000 title claims abstract description 27
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 27
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 100
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 78
- 239000007789 gas Substances 0.000 claims abstract description 21
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 15
- 239000010802 sludge Substances 0.000 claims description 24
- 239000002028 Biomass Substances 0.000 claims description 15
- 235000015097 nutrients Nutrition 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 235000016709 nutrition Nutrition 0.000 claims description 6
- 230000035764 nutrition Effects 0.000 claims description 6
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 10
- 239000001257 hydrogen Substances 0.000 description 8
- 229910052739 hydrogen Inorganic materials 0.000 description 8
- -1 meanwhile Chemical compound 0.000 description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 238000002485 combustion reaction Methods 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 231100000572 poisoning Toxicity 0.000 description 2
- 230000000607 poisoning effect Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 230000002194 synthesizing effect Effects 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- 206010021036 Hyponatraemia Diseases 0.000 description 1
- GCNLQHANGFOQKY-UHFFFAOYSA-N [C+4].[O-2].[O-2].[Ti+4] Chemical compound [C+4].[O-2].[O-2].[Ti+4] GCNLQHANGFOQKY-UHFFFAOYSA-N 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000618 nitrogen fertilizer Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000002686 phosphate fertilizer Substances 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/59—Biological synthesis; Biological purification
Landscapes
- 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 up 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) connects with being electrolysed the gas discharge outlet (4) of three rooms (2),Air inlet (3) connects with biogas shower nozzle (5),Each biogas shower nozzle (5) is provided with ignition (6),The circumferential periphery of the burner hearth of novel steam boiler (1) is provided with water tank (7),The water inlet of water tank (7) bottom connects with the delivery port of high-pressure hydraulic pump (12),The water inlet of high-pressure hydraulic pump (12) connects with running water pipe (13),The roof of the furnace of novel steam boiler (1) is provided with multiple high-temp waste gas discharge pipes (14),High-temp waste gas discharge pipe (14) connects with the air inlet (15) of methane phase room (16).
Description
Technical field
It the utility model is related to the setting that a kind of novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes zero-emission.
Background technology
It is well known that steam boiler, need to burn conventional energy resource, also discharge waste gas, pollute environment.Steam boiler one will be set
There is stockhole；Two will be provided 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.
The content of the invention
Technical problem to be solved in the utility model is that novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes zero
The setting of discharge.
The technical scheme in the invention for solving the technical problem is：
Novel steam boiler energy oxygen self-sufficiency waste gas circulation utilizes the setting of zero-emission.Because of steam copper in the market
Stove is designed with fire grate, clinker storage room, stockhole.And the burner hearth of the utility model steam boiler is closed, both without fire grate,
There is no clinker storage room, there is no stockhole also, do not enter air scoop, therefore claim novel steam boiler yet yet.Novel steam boiler energy
Oxygen self-sufficiency waste gas circulation in source utilizes the setting of zero-emission, is made up of Novel steam gas boiler and three Room of electrolysis.Novel steam kettle
The air inlet of stove connects with being electrolysed the gas discharge outlet of three Room.Air inlet connects with being located at the air inlet of biogas shower nozzle in burner hearth.
Bottom is provided with multiple biogas shower nozzles in burner hearth, and each biogas shower nozzle is provided with ignition.The burner hearth of novel steam boiler
Circumferential periphery is provided with water tank, and water tank is additionally provided with water-level gauge, air gauge, vapor outlet.Water tank periphery is provided with heat-insulation layer.Burner hearth
Interior top is provided with multiple S types heat-exchange tubes, and the suitable for reading and lower mouth of multiple S heat-exchange tubes connects with water tank respectively.Water tank bottom
Water inlet connected with the delivery port of high-pressure hydraulic pump, the water inlet of high-pressure hydraulic pump connects with running water pipe.Novel steam boiler
Roof of the furnace is provided with multiple high-temp waste gas discharge pipes, after multiple high-temp waste gas discharge pipes pass through water tank (7), is merged into a pipe,
The air inlet of methane phase room of the mouth of pipe with being electrolysed three Room connects.
As a kind of preferred scheme of the utility model device technique scheme, in addition to three Room of electrolysis are by methane phase room, the moon
Pole room, 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 also
Provided with sludge water outlet, sludge water outlet connects with hydraulic type biomass pool.The bottom of hydraulic type biomass pool is provided with into nutrition
Liquid mouth, enter nutrient solution mouth and connected with nutrition liquid pool.The bottom of hydraulic type biomass pool is additionally provided with sludge water outlet, sludge water discharge
Mouth and the sludge water inlet communication for being located at methane phase room bottom.Biogas delivery outlet, biogas output are provided with the top of hydraulic type biomass pool
Mouth connects with the air inlet of new normal-pressure boiler.
Operation principle：1st, the method that methane is produced in three Room of electrolysis, is comprised the following steps that：1. first will originally water electrolysis,
Or during because of sludge dilutional hyponatremia in hydraulic type biomass pool, the supernatant of unnecessary sludge water is extracted into filter, the water after filtering,
It is being electrolysed.Electrolysis water is stored in storage pool, the electrolysis water in storage pool, water tank is automatically injected by water pump.Setting in water tank
Ball valve, ball valve make water level be maintained at certain scope.Water tank connects with cathode chamber, anode chamber respectively.The position of water tank is higher than sun
The position of pole room, cathode chamber, certain hydraulic pressure is formed 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
Load nutrition liquid pool, mix, methane strain (under anaerobic environment, organic matter fermentation is over for methane strain) is 3. loaded into hydraulic pressure
Formula methane-generating pit, the nutrient solution in nutrition liquid pool is extracted into hydraulic type biomass pool with sewage pump, nutrient solution stirs evenly with methane strain, shape
Into 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
Room upper nozzle discharge, overflows to methane-generating pit, sludge water (methane strain) recycles.
2nd, include the waste gas of boiler engine exhaust, waste 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 connects with the bottom air inlet of methane phase room, and waste gas passes through
Gas distribution plate, rapid to rise evenly into methane phase room, now, water electrolyzer is started working, hydrogen caused by positive plate from
Son, hydrogen ion water is formed in anode chamber, first, the hydraulic pressure of the hydrogen ion water of anode chamber is more than the pressure of the sludge water of methane phase room,
Hydrogen ion water flows to methane phase room automatically in the presence of hydraulic pressure, by asymmetric barrier film, second, hydrogen ion water is inhaled in minus plate
Under drawing, by asymmetric electrolyte membrane into minus 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 waste gas, the work of carbon dioxide and hydrogen ion in methane backeria
Under, synthesizing methane, meanwhile, oxygen is also discharged, methane gas and oxygen rise, exported from gas delivery port, be transported to boiler
In internal combustion engine, methane acting (burning), oxygen participates in methane and done work (combustion-supporting), and waste gas circulation utilizes zero-emission, the hydrogen slipped through the net from
Son enters cathode chamber, and hydrogen ion is combined with hydrogen ion, generates hydrogen, and hydrogen rises, and by upper gas delivery outlet, is transported to pot
Stove internal combustion engine does work (burning), and waste gas circulation utilizes zero-emission.Oxonium ion caused by minus plate shifts to positive plate, in anode chamber
Oxonium ion is combined generation oxygen with oxonium ion, and oxygen rises, and is exported 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.
3rd, it is additionally included in methane phase room, methane backeria runs into oxonium ion, oxygen, and oxonium ion, oxygen poison methane backeria, part
It is rapid to rise after methane backeria poisoning, discharged from sludge water outlet, overflow 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.
4th, include the waste gas of boiler engine exhaust, in methane phase room with water electrolysis caused by hydrogen ion meet,
In the presence of methane backeria, synthesizing methane, meanwhile, oxygen is also discharged, hydrogen also caused by oxygen caused by anode chamber and cathode chamber
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, the anaerobic digestion resource circulation utilization cycle being formed, each element is recycled in closed container, not lost, therefore,
Boiler internal combustion engine can realize that the energy, oxygen are self-supporting, and waste gas circulation utilizes zero-emission.
Compared with prior art, the utility model one does not consume conventional energy resource；Two not oxygen in consumed cabin air；Three not to
Waste gas is discharged in air, can realize that the energy, oxygen are self-supporting, waste gas circulation utilizes zero-emission；
Brief description of the drawings
Fig. 1 is system schematic of the present utility model；
Embodiment
As illustrated, 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 form.The air inlet 3 of novel steam boiler 1 connects with being electrolysed the gas discharge outlet 4 of three Room 2, enters
Gas port 3 connects with being located at the air inlet of biogas shower nozzle 5 in burner hearth, and bottom is provided with multiple biogas shower nozzles 5, each biogas in burner hearth
Shower nozzle 5 is provided with ignition 6, and the circumferential periphery of the burner hearth of novel steam boiler 1 is provided with water tank 7, and water tank 7 is additionally provided with water-level gauge
8th, air gauge 9, vapor outlet 10, the top in burner hearth are provided with multiple S types heat-exchange tubes 11, multiple S heat-exchange tubes 11
Suitable for reading and lower mouth connects with water tank (7) respectively, and the water inlet of water tank (7) bottom connects with the delivery port of high-pressure hydraulic pump (12), high
The water inlet of water pump 12 is connected with running water pipe 13, and the roof of the furnace of novel steam boiler 1 is discharged provided with multiple high-temp waste gas
Manage (14), after multiple high-temp waste gas discharge pipes 14 pass through water tank 7, be merged into a pipe, the mouth of pipe and the methane phase room of three Room 2 of electrolysis
16 air inlet 15 connects.
Also include three Room 2 of electrolysis to be made up of methane phase room 16, cathode chamber 17, anode chamber 18, methane phase room 16, cathode chamber
17th, anode chamber 18 is respectively equipped with gas discharge outlet 4 at top, and the top of methane phase room 16 is additionally provided with sludge water outlet 19, sludge
Water outlet 19 is connected with hydraulic type biomass pool 20, and the bottom of hydraulic type biomass pool 20 is provided with into nutrient solution mouth 21, enters nutrient solution
Mouth 21 connects with 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
Connected with the sludge water inlet 24 for being located at the bottom of methane phase room 16, the top of hydraulic type biomass pool 20 is provided with biogas delivery outlet 25, natural pond
Gas delivery outlet 25 connects with the air inlet 3 of new 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, it is characterised 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) connect with being located at the air inlet of biogas shower nozzle (5) in burner hearth, and bottom is provided with multiple natural ponds in burner hearth
Gas blowout head (5), each biogas shower nozzle (5) are provided with ignition (6), and the circumferential periphery of the burner hearth of novel steam boiler (1) is set
There is a 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 provided with
Multiple S types heat-exchange tubes (11), the suitable for reading and lower mouth of multiple S heat-exchange tubes (11) connect with water tank (7) respectively, water tank (7) bottom
The water inlet in portion connects with the delivery port of high-pressure hydraulic pump (12), and the water inlet of high-pressure hydraulic pump (12) connects with running water pipe (13),
The roof of the furnace of novel steam boiler (1) is provided 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), a pipe is merged into, the air inlet (15) of methane phase room (16) of the mouth of pipe with being electrolysed three rooms (2) connects.
2. novel steam boiler energy oxygen self-sufficiency waste gas circulation according to claim 1 utilizes the setting of zero-emission, its
It is characterised by, in addition to electrolysis three rooms (2) is made up 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) connect with hydraulic type biomass pool (20), the bottom of hydraulic type biomass pool (20)
Portion is provided with into nutrient solution mouth (21), is entered nutrient solution mouth (21) and is connected 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 provided with biogas delivery outlet (25), biogas delivery outlet (25) and new normal-pressure boiler (1)
Air inlet (3) connects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720830941.7U CN206929758U (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 |
|---|---|---|---|
| CN201720830941.7U CN206929758U (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 |
|---|---|
| CN206929758U true CN206929758U (en) | 2018-01-26 |
Family
ID=61354745
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720830941.7U Expired - Fee Related CN206929758U (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) | CN206929758U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109554282A (en) * | 2018-03-01 | 2019-04-02 | 高节义 | Setting of the oxygenerator in conjunction with methane phase equipment |
-
2017
- 2017-06-28 CN CN201720830941.7U patent/CN206929758U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109554282A (en) * | 2018-03-01 | 2019-04-02 | 高节义 | Setting of the oxygenerator in conjunction with methane phase equipment |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180126 Termination date: 20180628 |
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| CF01 | Termination of patent right due to non-payment of annual fee |