CN205860013U - A kind of aqueous medium gasification combustion system - Google Patents
A kind of aqueous medium gasification combustion system Download PDFInfo
- Publication number
- CN205860013U CN205860013U CN201620874903.7U CN201620874903U CN205860013U CN 205860013 U CN205860013 U CN 205860013U CN 201620874903 U CN201620874903 U CN 201620874903U CN 205860013 U CN205860013 U CN 205860013U
- Authority
- CN
- China
- Prior art keywords
- electrode
- pressure
- pressurized tank
- dish
- catalysis
- 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.)
- Withdrawn - After Issue
Links
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Abstract
A kind of aqueous medium gasification combustion system, relate to burner apparatus, including pressure pump, air pump, pressurized tank, electrostatic generator, pressure controller and system controller, pressure controller is arranged on pressurized tank, system controller respectively with pressure pump, air pump, pressure controller is electrically connected, burner assembly is by catalysis electrode, electrode takes up dish, duct cover dish and insulated chassis composition, catalysis electrode and duct cover dish are arranged on electrode and take up on dish, electrode takes up dish and is arranged on insulated chassis, in the groove of insulated chassis, space constitutes pressure-bearing hydroecium, the water guide duct of catalysis electrode is communicated to pressure-bearing hydroecium, pressure-bearing hydroecium has water supply connector to access；The exhaust port of air pump is connected to the QI invigorating interface of pressurized tank, and the outlet of pressure pump is connected to the breathing interface bottom pressurized tank by check-valves, and the water supply connector of pressure-bearing hydroecium is connected on the pipeline breathed between interface of check-valves and pressurized tank.This utility model is with aqueous medium as gasified raw material, it is achieved cleaning burning, preserves the ecological environment.
Description
Technical field
This utility model relates to burner apparatus, especially relates to a kind of aqueous medium combustion apparatus.
Background technology
Water is a kind of material the abundantest containing protium, and each hydrone is by two hydrogen atoms and an oxygen atom knot
Conjunction forms, and containing the hydrogen more than 111 kilograms in every cubic meter of water, its quality capacity is more than 11.1%, and the calorific capacity of hydrogen is high, combustion
Burn 1 kg hydrogen and can release the heat of 142120kj, be three times of gasoline.Water is developed into a kind of energy apply, during burning
Not producing carbon dioxide, product only has water, can be repeatedly circulated, and to improving air acid rain environment, reduces dioxy in air
Change carbon content, thus alleviate greenhouse effect and have great benefit.Therefore, exploitation aqueous medium fuel not only can solve energy shortage
Situation, and environment protecting highlight.But, hydrogen atom and oxygen atom in hydrone combine the most firm, high-temperature heating
Method need to be heated to 3000 DEG C of decomposition carried out above hydrone, and general mode of heating is difficult to reach the highest temperature；Industry
Upper current method decomposition water molecule hydrogen manufacturing, decomposition rate is slow, efficiency is low, and it is the biggest to consume energy.
Utility model content
The purpose of this utility model is intended to overcome existing pyrolysis water hydrogen manufacturing and the shortcoming of current method decomposition water molecule hydrogen manufacturing, carries
For a kind of aqueous medium gasification combustion system, water is applied as a kind of energy, it is achieved cleaning burning, preserve the ecological environment.
A kind of aqueous medium gasification combustion system of the present utility model, occurs including pressure pump, air pump, pressurized tank, electrostatic
Device, pressure controller and system controller, pressure controller is arranged on pressurized tank, system controller respectively with pressure pump,
Air pump, pressure controller are electrically connected, and it is characterized in that there is burner assembly 1 in system, and burner assembly 1 is by catalysis electrode
1-4, electrode take up dish 1-1, duct cover dish 1-2 and insulated chassis 1-9 composition, and wherein, the upper semisection of catalysis electrode 1-4 is circular cone
Body structure, has water guide duct 1-401 in the lower half segment body of catalysis electrode 1-4；Have and catalysis electrode 1-4 phase on the cover dish 1-2 of duct
Duct 1-3 with quantity；In insulated chassis 1-9 fluted；Catalysis electrode 1-4 and duct cover dish 1-2 is arranged on electrode and takes up dish
On 1-1, the cone of catalysis electrode 1-4 upper semisection is placed among the duct 1-3 of duct cover dish 1-2；Electrode takes up dish 1-1 and installs
On insulated chassis 1-9 and be enclosed in groove port, in the groove of insulated chassis 1-9, space constitutes pressure-bearing hydroecium 21, catalysis electricity
The water guide duct 1-401 of pole 1-4 is communicated to pressure-bearing hydroecium 21, and pressure-bearing hydroecium 21 has water supply connector 1-8 to access；Dish is taken up at electrode
The inner side of 1-1 has metal backing 1-5, metal backing 1-5 to be connected to catalysis electrode 1-4, has conductive plug on metal backing 1-5
1-6, has electrically conductive socket 1-7 on insulated chassis 1-9, and the conductive plug 1-6 on metal backing 1-5 is inserted into insulated chassis 1-9
On electrically conductive socket 1-7 in, electrically conductive socket 1-7 is wired in anode interface 4-2 of electrostatic generator；Pressurized tank 15
Bottom have breathing interface 15-1 access, the lower side of pressurized tank 15 have survey water electrode 15-2 pick out, the top of pressurized tank 15
Side has QI invigorating interface 15-3 to access, and surveys water electrode 15-2 and is connected on the signal input part of system controller, the row of air pump 17
Gas interface is connected to the QI invigorating interface 15-3 of pressurized tank 15, and the outlet of pressure pump 7 is connected to pressurized tank by check-valves 11
Breathing interface 15-1 bottom 15, the water supply connector 1-8 of pressure-bearing hydroecium 21 are connected to the breathing of check-valves 11 and pressurized tank 15 and connect
On pipeline between mouth 15-1.
In this utility model, catalysis electrode 1-4 is metal powder sintered microporous filter membrane structure, and catalysis electrode 1-4 is constituted
Hydrone filters and catalysis element, and when being embodied as, catalysis electrode 1-4 is that the material of tungsten powder and the mixing of nickel-sulfur alloy powder burns
Form tungsten nickel pseudo-alloy part, when firing, tungsten, nickel-sulfur alloy neither mutual phased soln, also it is formed without intermetallic compound, is formed
Pseudo-alloy be organized as two phase structures of tungsten particle, nickel-sulfur alloy granule, pseudo-alloy tissue exists micro-pore, micro-pore
Constituting the filtration channel of hydrone, have the effect filtering hydrone, the decomposition of hydrone is had by nickel-sulfur alloy therein urges
Change effect, makes hydrone be easier to decompose；Catalysis electrode 1-4 is more than one, and many catalysis electrodes are evenly distributed on electrode and hold
On sabot 1-1；Duct 1-3 on the cover dish 1-2 of duct is up-small and down-big inverted tubaeform structure, and catalysis electrode 1-4 covers with duct
Having space between duct 1-3 wall body on dish 1-2, the space between the wall body of catalysis electrode 1-4 and duct 1-3 constitutes electrostatic
?；Duct cover dish 1-2 is electrically connected with the negative pole interface of electrostatic generator；Take up at electrode and on dish 1-1, have normally closed aerofluxus
Valve 23, normally closed air bleeding valve 23 is communicated to pressure-bearing hydroecium 21；The pipeline that pressure pump 7 accesses there is water purifier 9.
This utility model is suitable on Industrial Boiler application, with aqueous medium as gasified raw material, it is achieved cleaning burning, obtains heat
Can, during application, pressure pump, air pump 17, pressurized tank, electrostatic generator, system controller 6 and burner assembly 1 are installed each
Frame on.During work, the electrostatic that catalysis electrode 1-4 and duct cover dish 1-2 is applied more than 10,000 volts, make catalysis electrode 1-4's
Upper semisection cone is in the electrostatic field among the 1-3 of duct, to increase the catalysis activity of catalysis electrode 1-4, and to moisture
Son forms ionization；Using pure water as raw water, the pressurized water pump of raw water 7 enters into the pressure-bearing of burner assembly 1
In hydroecium 21, raw water is entered in pressurized tank by the breathing interface 15-1 bottom pressurized tank 15 simultaneously, and make in pressurized tank 15 is upper
Portion's air is compressed, and forms compressed air, and the water of pressurized tank 15 bottom has pressure, artesian water under compressed-air actuated effect
Hydraulic pressure in room 21 is equal with the hydraulic pressure of pressurized tank 15 bottom.There is the pure water of pressure by water guide duct in pressure-bearing hydroecium 21
1-401 penetrates in the micro-pore of catalysis electrode 1-4, and hydrone is filtered by the micro-pore of catalysis electrode 1-4, makes big
Micel becomes little molecule, and the activity of hydrone is improved, and makes hydrone be easier to be decomposed, meanwhile, and catalysis electrode 1-4
Nickel-sulfur alloy material hydrone is carried out catalytic decomposition.Hydrone, through pressure permeation, is changed into little point by macromolecular mass
Sub-unity structure, then ionize through the catalysis of nickel-sulfur alloy material and electrostatic field, it is decomposed into hydrogen, oxygen and active hydrogen atom, activity
Oxygen atom, the activity chemistry thing of reactive hydrogen oxygen atomic group, escape from the upper semisection cone of catalysis electrode 1-4, become gasification
Fuel, enters in the 1-3 of duct, and the vaporising fuel that hydrone converts is by the high pressure between catalysis electrode 1-4 and duct 1-3 wall body
Spark ignition, carries out back reaction burning, releases heat energy.In said process, the operation pressure in pressurized tank 15 is by Stress control
The signal of device 18 is input to the signal of system controller 6 and survey water electrode 15-2 and is input to system controller 6, by system control
Device 6 is controlled, and when the water in pressurized tank 15 is consumed, the pressure in pressurized tank 15 can decrease, when in pressurized tank 15
Pressure less than pressure controller 18 set threshold pression and pressurized tank 15 in water level less than survey water electrode 15-2 time, system control
The power supply of pressure pump 7 connected by device 6 processed, makes pressure pump 7 run, and carries out moisturizing to pressurized tank 15, makes the sky in pressurized tank 15
Air pressure contracts and makes pressure inside the tank raise；When the pressure in pressurized tank 15 is less than threshold pression and the pressure that pressure controller 18 sets
Water level in tank 15 is higher than when surveying water electrode 15-2, and system controller 6 is connected the power supply of air pump 17, made air pump 17 run, to pressure
In power tank 15, input compressed air, makes the pressure in pressurized tank 15 raise；When the pressure in pressurized tank 15 reaches the upper limit of setting
During pressure, system controller 6 disconnects pressure pump 7 or the power supply of air pump 17, makes pressure pump 7 or air pump 17 stop, by being
The control of system controller 6, keeps pressure and water level constant in the range of setting in making pressurized tank 15.Pressure-bearing of the present utility model
The water of the water in hydroecium 21 and infiltration catalysis electrode 1-4 produces cooling effect to catalysis electrode 1-4, and protection catalysis electrode 1-4 is not
It is burned.This utility model use electrostatic improve catalysis electrode 1-4 catalysis activity and utilize electrostatic field to ionize hydrone,
Reducing the temperature requirement of pyrolysis hydrone, institute's consuming electric power is few, and the decomposition efficiency of hydrone is high.
This utility model takes up at electrode normally closed air bleeding valve 23 on dish 1-1, when using for the first time, open normally closed air bleeding valve
23, the air in pressure-bearing hydroecium 21 is discharged with water inlet, and it is easy to make into water.
The beneficial effects of the utility model are: a kind of aqueous medium gasification combustion system of offer, are suitable on Industrial Boiler
Application, with aqueous medium as gasified raw material, hydrone by pressure permeation, is changed into small molecular cluster structure by macromolecular mass, then
Ionizing through the catalysis of nickel-sulfur alloy material and electrostatic field, the vaporising fuel being decomposed into hydrogen-oxygen burns, using water as a kind of energy
Apply, it is achieved cleaning burning, preserve the ecological environment.
Accompanying drawing explanation
Fig. 1 is the structure chart of a kind of aqueous medium gasification combustion system of the present utility model.
Fig. 2 is the attached view of burner assembly of the present utility model.
Fig. 3 is the enlarged drawing of catalysis electrode of the present utility model.
In figure: 1. burner assembly, 1-1. electrode takes up dish, 1-2. duct cover dish, 1-3. duct, 1-4. catalysis electrode,
1-401. water guide duct, 1-402. outer-hexagonal body, 1-403. external screw thread, 1-404. micropore cone, 1-5. metal backing, 1-6.
Conductive plug, 1-7. electrically conductive socket, 1-8. water supply connector, 1-9. insulated chassis, 2. fastening bolt, 3. wire, 4. electrostatic occurs
Device, 4-1. negative pole interface, 4-2. anode interface, 5. penstocks, 6. system controller, 7. pressure pump, 8. communicating pipe, the cleanest
Hydrophone, 10. feed pipe, 11. check-valves, 12. threeways, 13. frames, 14. pressure pure water, 15. pressurized tanks, 15-1. breathes and connects
Mouthful, 15-2. surveys water electrode, 15-3. QI invigorating interface, 15-4. satellite interface, 16. compressed airs, 17. air pumps, 18. Stress control
Device, 19. threeways, 20. maintenance exhaust-valves, 21. pressure-bearing hydroeciums, 22. sealing gaskets, 23. normally closed air bleeding valves.
Detailed description of the invention
In embodiment shown in embodiment 1 Fig. 1, a kind of aqueous medium gasification combustion system mainly by burner assembly 1,
Pressure pump 7, air pump 17, pressurized tank 15, electrostatic generator 4, pressure controller 18 and system controller 6 form, Stress control
Device 18 is arranged on pressurized tank 15, and system controller 6 electrically connects with pressure pump 7, air pump 17, pressure controller 18 respectively
Connecing, burner assembly 1 is taken up dish 1-1 by catalysis electrode 1-4, electrode, duct cover dish 1-2 and insulated chassis 1-9 forms, wherein,
The upper semisection of catalysis electrode 1-4 is conical structure, has water guide duct 1-401 in the lower half segment body of catalysis electrode 1-4；Duct is covered
Having on dish 1-2 and the duct 1-3 of catalysis electrode 1-4 equal number, duct 1-3 is up-small and down-big inverted tubaeform structure；Insulation
In the 1-9 of chassis fluted；Catalysis electrode 1-4 and duct cover dish 1-2 is arranged on electrode and takes up on dish 1-1, and catalysis electrode 1-4 is one
More than Zhi, many catalysis electrodes are evenly distributed on electrode and take up on dish 1-1, and the cone of catalysis electrode 1-4 upper semisection is placed in hole
Among the duct 1-3 of road cover dish 1-2, between the duct 1-3 wall body on catalysis electrode 1-4 and duct cover dish 1-2, there is space, catalysis
Space between the wall body of electrode 1-4 and duct 1-3 constitutes electrostatic field；Electrode takes up dish 1-1 and is arranged on insulated chassis 1-9 also
Being enclosed in groove port, in the groove of insulated chassis 1-9, space constitutes pressure-bearing hydroecium 21, the water guide duct 1-of catalysis electrode 1-4
401 are communicated to pressure-bearing hydroecium 21, and pressure-bearing hydroecium 21 has water supply connector 1-8 to access；There is metal liner the inner side taking up dish 1-1 at electrode
Plate 1-5, metal backing 1-5 are connected to catalysis electrode 1-4, have conductive plug 1-6 on metal backing 1-5, at insulated chassis 1-9
On have electrically conductive socket 1-7, the conductive plug 1-6 on metal backing 1-5 is inserted in the electrically conductive socket 1-7 on insulated chassis 1-9,
Electrically conductive socket 1-7 is wired in anode interface 4-2 of electrostatic generator, duct cover dish 1-2 and electrostatic generator
Negative pole interface is electrically connected；The bottom of pressurized tank 15 has breathing interface 15-1 to access, and the lower side of pressurized tank 15 has survey
Water electrode 15-2 picks out, and the upper side of pressurized tank 15 has QI invigorating interface 15-3 to access, and surveys water electrode 15-2 and is connected to system control
On the signal input part of device processed, the exhaust port of air pump 17 is connected to the QI invigorating interface 15-3 of pressurized tank 15, going out of pressure pump 7
The mouth of a river is connected to the breathing interface 15-1 bottom pressurized tank 15 by check-valves 11, and the water supply connector 1-8 of pressure-bearing hydroecium 21 connects
On pipeline between the breathing interface 15-1 of check-valves 11 and pressurized tank 15.In the present embodiment, take up at electrode and have on dish 1-1
Normally closed air bleeding valve 23, normally closed air bleeding valve 23 is communicated to pressure-bearing hydroecium 21；The pipeline that pressure pump 7 accesses there is water purifier 9；Urge
Polarizing electrode 1-4 is metal powder sintered microporous filter membrane structure, and catalysis electrode 1-4 constitutes hydrone and filters and catalysis element, urges
Polarizing electrode 1-4 is that the material of tungsten powder and the mixing of nickel-sulfur alloy powder sinters tungsten nickel pseudo-alloy part, when firing, tungsten, nickel sulfur into
Alloy neither mutual phased soln, is also formed without intermetallic compound, and the pseudo-alloy formed is organized as tungsten particle, nickel-sulfur alloy granule
Two phase structures, pseudo-alloy tissue exists micro-pore, micro-pore constitutes the filtration channel of hydrone, has filtration moisture
The effect of son, nickel-sulfur alloy therein has catalytic action to the decomposition of hydrone, makes hydrone be easier to decompose；Electrode takes up
Dish 1-1 and insulated chassis 1-9 selects alumina ceramic material or zirconia ceramics material to make, and duct cover dish 1-2 selects stainless
Steel material makes.
The present embodiment uses in Industrial Boiler, and burner assembly 1 is arranged in the burner hearth of Industrial Boiler, to duct cover dish
1-2 carries out ground protection process, pressure pump 7, air pump 17, pressurized tank 15, electrostatic generator 4, pressure controller 18 and system
Controller 6 is arranged on the periphery of Industrial Boiler.During work, catalysis electrode 1-4 and duct cover dish 1-2 is applied more than 10,000 volts
Electrostatic, makes the upper semisection cone of catalysis electrode 1-4 be in the electrostatic field among the 1-3 of duct, to increase catalysis electrode 1-4's
Catalysis activity, and hydrone is formed ionization；Using pure water as raw water, the pressurized water pump of raw water 7 enters
In the pressure-bearing hydroecium 21 of burner assembly 1, raw water is entered pressurized tank by the breathing interface 15-1 bottom pressurized tank 15 simultaneously
In, making the upper air in pressurized tank 15 be compressed, form compressed air, the water of pressurized tank 15 bottom is at compressed-air actuated work
Having pressure under with, the hydraulic pressure in pressure-bearing hydroecium 21 is equal with the hydraulic pressure of pressurized tank 15 bottom.In pressure-bearing hydroecium 21, there is pressure
Pure water penetrated in the micro-pore of catalysis electrode 1-4 by water guide duct 1-401, the micro-pore of catalysis electrode 1-4
Filtering hydrone, make macromolecular mass become little molecule, the activity of hydrone is improved, and makes hydrone be easier to obtain
Decomposing, meanwhile, the nickel-sulfur alloy material of catalysis electrode 1-4 carries out catalytic decomposition to hydrone.Hydrone through pressure permeation,
It is changed into small molecular cluster structure by macromolecular mass, then ionizes through the catalysis of nickel-sulfur alloy material and electrostatic field, be decomposed into hydrogen, oxygen
And the activity chemistry thing of active hydrogen atom, active oxygen atom, reactive hydrogen oxygen atomic group, from the upper semisection circle of catalysis electrode 1-4
Escaping in cone, become vaporising fuel, enter in the 1-3 of duct, the vaporising fuel that hydrone converts is by catalysis electrode 1-4 and hole
High-voltage spark between road 1-3 wall body is lighted, and carries out back reaction burning, releases heat energy.In said process, in pressurized tank 15
The signal that operation pressure is input to system controller 6 and survey water electrode 15-2 by the signal of pressure controller 18 is input to system
Controller 6, is controlled by system controller 6, and when the water in pressurized tank 15 is consumed, the pressure in pressurized tank 15 can drop therewith
Low, when the pressure in pressurized tank 15 less than pressure controller 18 set threshold pression and pressurized tank 15 in water level less than survey water
During electrode 15-2, system controller 6 connects the power supply of pressure pump 7, makes pressure pump 7 run, and carries out moisturizing to pressurized tank 15,
The compression of the air in pressurized tank 15 is made to make pressure inside the tank raise；When the pressure in pressurized tank 15 sets less than pressure controller 18
Threshold pression and pressurized tank 15 in water level higher than survey water electrode 15-2 time, system controller 6 is connected the power supply of air pump 17, is made
Air pump 17 runs, and to input compressed air in pressurized tank 15, makes the pressure in pressurized tank 15 raise；Pressure in pressurized tank 15
When reaching the pressure upper limit set, system controller 6 disconnects pressure pump 7 or the power supply of air pump 17, makes pressure pump 7 or air pump
17 stop, and by the control of system controller 6, keep pressure and water level constant in the range of setting in making pressurized tank 15.This
Embodiment, when using for the first time, opens normally closed air bleeding valve 23, and the air in pressure-bearing hydroecium 21 is discharged with water inlet, makes to hold into water
Easily.
Claims (7)
1. an aqueous medium gasification combustion system, including pressure pump, air pump, pressurized tank, electrostatic generator, pressure controller and
System controller, pressure controller is arranged on pressurized tank, system controller respectively with pressure pump, air pump, pressure controller
Being electrically connected, it is characterized in that there is burner assembly (1) in system, burner assembly (1) is by catalysis electrode (1-4), electrode
Taking up dish (1-1), duct cover dish (1-2) and insulated chassis (1-9) composition, wherein, the upper semisection of catalysis electrode (1-4) is circular cone
Body structure, has water guide duct (1-401) in the lower half segment body of catalysis electrode (1-4)；Have and catalysis electrode on duct cover dish (1-2)
(1-4) duct (1-3) of equal number；In insulated chassis (1-9) fluted；Catalysis electrode (1-4) and duct cover dish (1-2) peace
Being contained in electrode and take up on dish (1-1), the cone of catalysis electrode (1-4) upper semisection is placed in the duct (1-3) in duct cover dish (1-2)
Among；Electrode takes up dish (1-1) and is arranged on insulated chassis (1-9) and is enclosed in groove port, the groove of insulated chassis (1-9)
Interior space constitutes pressure-bearing hydroecium (21), and the water guide duct (1-401) of catalysis electrode (1-4) is communicated to pressure-bearing hydroecium (21), pressure-bearing
Hydroecium (21) has water supply connector (1-8) to access；There are metal backing (1-5), metal backing in the inner side taking up dish (1-1) at electrode
(1-5) it is connected to catalysis electrode (1-4), metal backing (1-5) has conductive plug (1-6), insulated chassis (1-9) has
Electrically conductive socket (1-7), the conductive plug (1-6) on metal backing (1-5) is inserted into the electrically conductive socket on insulated chassis (1-9)
(1-7), in, electrically conductive socket (1-7) is wired in the anode interface (4-2) of electrostatic generator；The end of pressurized tank (15)
Portion has breathing interface (15-1) to access, and the lower side of pressurized tank (15) has survey water electrode (15-2) to pick out, pressurized tank (15)
Upper side has QI invigorating interface (15-3) to access, and surveys water electrode (15-2) and is connected on the signal input part of system controller, gas
The exhaust port of pump (17) is connected to the QI invigorating interface (15-3) of pressurized tank (15), and the outlet of pressure pump (7) passes through non-return
Valve (11) is connected to the breathing interface (15-1) of pressurized tank (15) bottom, and the water supply connector (1-8) of pressure-bearing hydroecium (21) is connected to
On pipeline between the breathing interface (15-1) of check-valves (11) and pressurized tank (15).
A kind of aqueous medium gasification combustion system the most according to claim 1, is characterized in that catalysis electrode (1-4) is metal powder
The microporous filter membrane structure of end sintering, catalysis electrode (1-4) constitutes hydrone and filters and catalysis element.
A kind of aqueous medium gasification combustion system the most according to claim 1, it is characterized in that catalysis electrode (1-4) be one with
On, many catalysis electrodes are evenly distributed on electrode and take up on dish (1-1).
A kind of aqueous medium gasification combustion system the most according to claim 1, is characterized in that the duct on duct cover dish (1-2)
(1-3) be up-small and down-big inverted tubaeform structure, duct (1-3) wall body on catalysis electrode (1-4) and duct cover dish (1-2) it
Between have space, space between the wall body of catalysis electrode (1-4) and duct (1-3) constitutes electrostatic field.
A kind of aqueous medium gasification combustion system the most according to claim 1, is characterized in that duct cover dish (1-2) is sent out with electrostatic
The negative pole interface of raw device is electrically connected.
A kind of aqueous medium gasification combustion system the most according to claim 1, is characterized in that taking up at electrode have on dish (1-1)
Normally closed air bleeding valve (23), normally closed air bleeding valve (23) is communicated to pressure-bearing hydroecium (21).
A kind of aqueous medium gasification combustion system the most according to claim 1, is characterized in that at the pipe that pressure pump (7) accesses
Water purifier (9) is had on road.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620874903.7U CN205860013U (en) | 2016-08-15 | 2016-08-15 | A kind of aqueous medium gasification combustion system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620874903.7U CN205860013U (en) | 2016-08-15 | 2016-08-15 | A kind of aqueous medium gasification combustion system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205860013U true CN205860013U (en) | 2017-01-04 |
Family
ID=57593642
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620874903.7U Withdrawn - After Issue CN205860013U (en) | 2016-08-15 | 2016-08-15 | A kind of aqueous medium gasification combustion system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205860013U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106090910A (en) * | 2016-08-15 | 2016-11-09 | 衢州昀睿工业设计有限公司 | A kind of aqueous medium gasification combustion system |
-
2016
- 2016-08-15 CN CN201620874903.7U patent/CN205860013U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106090910A (en) * | 2016-08-15 | 2016-11-09 | 衢州昀睿工业设计有限公司 | A kind of aqueous medium gasification combustion system |
| CN106090910B (en) * | 2016-08-15 | 2017-11-24 | 衢州昀睿工业设计有限公司 | A kind of aqueous medium gasification combustion system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203685418U (en) | Vehicle oxyhydrogen maintaining fuel-saving system | |
| CN205860013U (en) | A kind of aqueous medium gasification combustion system | |
| CN201373545Y (en) | Oxy-hydrogen gas water heater | |
| CN204591541U (en) | A kind of mine air-lack that utilizes is as the internal combustion engine power generating system of fuel | |
| CN205855992U (en) | Aqueous medium gasified combustion apparatus | |
| US9341112B2 (en) | Combination air pressure system and plasma ion gas generator system for turbocharged diesel engine | |
| CN106765089A (en) | A kind of gas-cooker and control method with plasma generator | |
| CN104544565A (en) | Suction liquid feeding electronic cigarette | |
| CN205990231U (en) | The producing and burner of aqueous medium fuel | |
| CN106090910B (en) | A kind of aqueous medium gasification combustion system | |
| CN201525892U (en) | Hydrogen and oxygen generator for burning aid | |
| CN106082124B (en) | A kind of burner of aqueous medium conversion fuel | |
| CN106145032B (en) | Aqueous medium gasified combustion apparatus | |
| TWI573761B (en) | Hydrogen carbon cleaning method for vehicle | |
| CN205860455U (en) | Aqueous medium converts the water heater of fuel | |
| CN106082123B (en) | Aqueous medium fuel produce and burner | |
| CN105927982B (en) | Hydrogen and oxygen mixture combustion system | |
| CN106152472A (en) | Aqueous medium converts the water heater of fuel | |
| CN105219462B (en) | Modified HCNG fuel process and preparation system | |
| CN205687549U (en) | A kind of gas water separation tank on oxyhydrogen generator | |
| CN1995818B (en) | Aqueous oxyhydrogen source gas burner multipurpose machine | |
| CN208074948U (en) | A kind of combustion system of electrolysis HHO fuel | |
| CN104296157B (en) | A kind of water fuel hydrogen oxygen and aiding combustion boiler | |
| CN205528641U (en) | Modified HCNG fuel preparation system | |
| CN205560715U (en) | Burner that industrial boiler used |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170104 Effective date of abandoning: 20171124 |
|
| AV01 | Patent right actively abandoned |