CN108264020A - A kind of water-gas hydrogen producer - Google Patents
A kind of water-gas hydrogen producer Download PDFInfo
- Publication number
- CN108264020A CN108264020A CN201810119694.9A CN201810119694A CN108264020A CN 108264020 A CN108264020 A CN 108264020A CN 201810119694 A CN201810119694 A CN 201810119694A CN 108264020 A CN108264020 A CN 108264020A
- Authority
- CN
- China
- Prior art keywords
- gas
- carbon dioxide
- water
- chamber
- hydrogen
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/12—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with carbon monoxide
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D7/00—Fertilisers producing carbon dioxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
Abstract
The invention discloses a kind of water-gas hydrogen producers, including apparatus main body, the carbon dioxide adsorption device being set in described device main body, the water-gas vapor reaction unit being set on the left of described device main body and the Hydrogen collection device being set on the right side of described device main body, the water-gas vapor reaction unit includes retort, water-gas vapor reaction chamber is provided in the retort, the water-gas vapor reaction chamber inner left wall is provided with the water-gas air inlet pipe being connected with the water-gas vapor reaction chamber, water-gas air inlet switch is provided in the water-gas air inlet pipe, the water-gas vapor reaction chamber upper inside walls are provided with the vapor air inlet pipe being connected with the water-gas vapor reaction chamber, vapor air inlet switch is provided in the vapor air inlet pipe.
Description
Technical field
The present invention relates to water-gas hydrogen producing technology field, specifically a kind of water-gas hydrogen producer.
Background technology
China is energy consumption big country in the world, and annual industrial production, automobile etc. all consumes a large amount of oil, simultaneously
Also it has given off a large amount of polluted gas and has so produced a large amount of chain reaction, for example greenhouse effects are increasingly severe
Deng, therefore national governments are also actively seeking other clean energy resourcies to reduce the discharge of polluted gas and now be considered as clear
The water-gas gas of the clean energy equally can also generate a large amount of carbon dioxide when in use, and certain influence can be also generated to air,
And hydrogen react when only need oxygen consumption gas and generate moisture, can direct emission any dirt will not be generated in air and to air
Dye, therefore replace the fuel such as previous petroleum gas that there is very good development prospect using hydrogen, therefore design a kind of
Water-gas hydrogen producer it is really necessary to.
Invention content
The technical problems to be solved by the invention are to provide a kind of water-gas hydrogen producer, can solve above-mentioned present skill
The problems in art.
The present invention is achieved through the following technical solutions：A kind of water-gas hydrogen producer of the present invention, including device
Main body, the carbon dioxide adsorption device being set in described device main body, the water-gas-water being set on the left of described device main body
Vapor reaction device and the Hydrogen collection device being set on the right side of described device main body, the water-gas-vapor reaction dress
It puts including retort, water-gas-vapor reaction chamber is provided in the retort, the water-gas-vapor reaction chamber is left
Side inner wall is provided with the water-gas air inlet pipe being connected with the water-gas-vapor reaction chamber, in the water-gas air inlet pipe
Water-gas air inlet switch is provided with, the water-gas-vapor reaction chamber upper inside walls are provided with and the water-gas-vapor
The vapor air inlet pipe that reaction chamber is connected is provided with vapor air inlet switch, the retort in the vapor air inlet pipe
Right side is provided with apparatus main body, and carbon dioxide adsorption device, the carbon dioxide adsorption device are provided in described device main body
Including the carbon dioxide adsorption chamber being set in described device main body, the company of being provided between described device main body and the retort
Lead to the ventilation pipe of the water-gas-vapor reaction chamber and the carbon dioxide adsorption chamber, be provided on the ventilation pipe
Fan device is evacuated, is fixedly installed fan electromotor in the carbon dioxide adsorption chamber upper inside walls, the fan electromotor lower end leads to
It crosses shaft power and is connected with fan blade, be provided with and the carbon dioxide in the inner wall of the carbon dioxide adsorption chamber downside
The carbon dioxide outlet pipe that adsorbent chamber is connected, the carbon dioxide outlet pipe are connected with the carbon dioxide adsorption chamber
Place is provided with ramp structure, and carbon dioxide is provided on the carbon dioxide outlet pipe and goes out air cock, described device main body is right
Side is provided with Hydrogen collection device, and the Hydrogen collection device is connected to described device main body right end face including secure fit
Main body is collected, Hydrogen collection chamber is provided in the collection main body, is the titanium dioxide in the Hydrogen collection chamber inner left wall
The outlet pipe for connecting the Hydrogen collection chamber and the carbon dioxide adsorption chamber is provided on the right side of carbon adsorption chamber in inner wall, it is described
Outlet pipe is provided with carbon dioxide adsorption block, the Hydrogen collection chamber upper inside walls with the carbon dioxide adsorption chamber junction
Ramp is provided with, the ramp medium position is provided with the hydrogen outlet pipe being connected with the Hydrogen collection chamber, institute
It states and hydrogen is provided on hydrogen outlet pipe goes out air cock, the hydrogen outlet pipe is set with the Hydrogen collection chamber junction
There are dried pieces, Hydrogen collection chamber downside inner wall is provided with lower inclined plane, and the lower inclined plane medium position is provided with and the hydrogen
The miscellaneous gas outlet pipe that gas collecting chamber is connected is provided with miscellaneous gas on the miscellaneous gas outlet pipe and goes out air cock；Described device master
Heat extraction component is provided in body, the heat extraction component includes the annular groove for being arranged on the fan electromotor periphery, set in the annular groove
The heat dissipating ring being bonded with the fan electromotor outer surface is equipped with, the heat emission hole communicated up and down is provided in the heat dissipating ring, it is described
Annular groove left end is provided with and air inlet duct is communicated with outside, and exhaust fan, the annular groove right end setting are installed in the air inlet duct
Have with the outgassing groove that communicates of outside, generated heat is arranged during so as to run by the exhaust fan by the fan electromotor
Go out, the accumulation of heat can be avoided.
First is respectively arranged with as preferred technical solution, before and after the water-gas-vapor reaction chamber in inner wall to add
Hot chamber is provided with the first resistive heater in first heating chamber.
As preferred technical solution, the carbon dioxide adsorption chamber is set respectively in the front and rear inner wall of downside inner wall
There is the second heating chamber, the second resistive heater is provided in second heating chamber.
As preferred technical solution, the medium position of inner wall is fixedly installed dioxy on the right side of the carbon dioxide adsorption chamber
Change concentration of carbon detection device, when the carbon dioxide adsorption intracavitary gas concentration lwevel reaches designated value, the carbon dioxide
Concentration detection apparatus controls the fan electromotor rotation, and the gas that carbon dioxide adsorption intracavitary contains high concentration carbon dioxide is led to
The carbon dioxide outlet pipe is crossed to be blown out in specified containers.
The beneficial effects of the invention are as follows：The configuration of the present invention is simple, it is easy to operate, the behaviour of hydrogen making is carried out by the present apparatus
Make process, water-gas air inlet pipe is connected on the container of storage water-gas by user of service, and opening water-gas air inlet switch at this time will
Water-gas is filled in water-gas-vapor reaction chamber, opens simultaneously vapor air inlet switch, by vapor air inlet pipe to water coal
Air-water vapor reaction intracavitary injects vapor, is powered at this time to the first resistive heater and passes through the first resistive heater by water
Temperature in coal gas-vapor reaction chamber is heated to 427 degrees Celsius, the carbon monoxide in the water-gas injected at this time
It reacts the carbon dioxide and hydrogen of generation same volume at high operating temperatures with vapor, treats gas in water-gas-vapor reaction chamber
It after body reacts to greatest extent, is set to pumping fan device on ventilation pipe and starts, and by water-gas-vapor reaction chamber
Interior gas pumps to carbon dioxide adsorption intracavitary and the carbon dioxide adsorption block by being set in outlet pipe enters hydrogen
In gas collecting chamber, enter at this time carbon dioxide adsorption intracavitary gas include the hydrogen of most of volume, carbon dioxide with
And the carbon monoxide reacted completely, the vapor of not a small amount of volume, when gas passes through carbon dioxide adsorption block, two in gas
Carbonoxide is blocked in the carbon dioxide adsorption intracavitary on the left of carbon dioxide adsorption block by carbon dioxide adsorption block, when carbon dioxide is inhaled
When the gas concentration lwevel of attached intracavitary reaches certain value, carbon dioxide concentration detecting device control fan electromotor rotation is given simultaneously
Second resistive heater is powered, and is heated to coming off carbon dioxide adsorption block simultaneously by the carbon dioxide particle of carbon dioxide adsorption intracavitary
Carbon dioxide blowout carbon dioxide outlet pipe is entered in specified containers by fan blade, the titanium dioxide being collected at this time
Carbon can be used as the Fertilizer application of booth vegetable, and enter the gas of Hydrogen collection intracavitary for hydrogen and a small amount of by outlet pipe
Carbon monoxide and vapor, since the relative molecular mass of hydrogen is much smaller than the relative molecular mass of carbon monoxide and vapor,
Therefore hydrogen floats on upper strata in Hydrogen collection intracavitary, and carbon monoxide and vapor are then deposited on the bottom of Hydrogen collection chamber,
Opening hydrogen, which goes out air cock, at this time to extract the hydrogen of Hydrogen collection intracavitary out, the Hydrogen collection intracavitary after one end time is used
Miscellaneous gas become more, therefore need to periodically open miscellaneous gas and go out air cock by the releasing of the miscellaneous gas of Hydrogen collection intracavitary to prevent from passing through the present apparatus
The density of hydrogen of collection reduces.
Description of the drawings
For ease of explanation, the present invention is described in detail by following specific embodiment and attached drawing.
Fig. 1 is a kind of internal structure schematic diagram of water-gas hydrogen producer of the present invention；
Fig. 2 is the schematic diagram in " A-A " direction in Fig. 1；
Fig. 3 is the structure diagram of the first heating chamber of the present invention.
Specific embodiment
As shown in Figure 1-Figure 3, a kind of water-gas hydrogen producer of the invention, including apparatus main body 11, is set to the dress
Put the carbon dioxide adsorption device in main body 11, the water-gas-vapor reaction unit for being set to 11 left side of described device main body
And the Hydrogen collection device on 11 right side of described device main body is set to, the water-gas-vapor reaction unit includes reaction
Tank 25 is provided with water-gas-vapor reaction chamber 26,26 left side of the water-gas-vapor reaction chamber in the retort 25
Inner wall is provided with the water-gas air inlet pipe 21 being connected with the water-gas-vapor reaction chamber 26, the water-gas air inlet pipe
Water-gas air inlet switch 22 is provided on 21, the water-gas -26 upper inside walls of vapor reaction chamber are provided with and the water coal
The vapor air inlet pipe 23 that air-water vapor reaction chamber 26 is connected is provided with vapor air inlet in the vapor air inlet pipe 23
Switch 24,25 right side of retort are provided with apparatus main body 11, carbon dioxide adsorption dress are provided in described device main body 11
It puts, the carbon dioxide adsorption device includes the carbon dioxide adsorption chamber 36 being set in described device main body 11, described device
It is provided between main body 11 and the retort 25 and connects the water-gas-vapor reaction chamber 26 and the carbon dioxide adsorption
The ventilation pipe 32 of chamber 36 is provided with pumping fan device 31,36 upside of carbon dioxide adsorption chamber on the ventilation pipe 32
Fan electromotor 33 is fixedly installed in inner wall, 33 lower end of fan electromotor is connected with fan blade by 34 power of shaft
35, the carbon dioxide being connected with the carbon dioxide adsorption chamber 36 is provided in the 36 downside inner wall of carbon dioxide adsorption chamber
Outlet pipe 43, the carbon dioxide outlet pipe 43 are provided with ramp structure with 36 connection of carbon dioxide adsorption chamber
42, carbon dioxide is provided on the carbon dioxide outlet pipe 43 and goes out air cock 45,11 right side of described device main body is provided with
Hydrogen collection device, the Hydrogen collection device include the collection master that secure fit is connected to 11 right end face of described device main body
Body 12, described collect are provided with Hydrogen collection chamber 64 in main body 12, be the dioxy in 64 inner left wall of Hydrogen collection chamber
Change in 36 right side inner wall of carbon adsorption chamber and be provided with the outlet for connecting the Hydrogen collection chamber 64 and the carbon dioxide adsorption chamber 36
Pipeline 46, the outlet pipe 46 is provided with carbon dioxide adsorption block 41 with 36 junction of carbon dioxide adsorption chamber, described
64 upper inside walls of Hydrogen collection chamber are provided with ramp 63, and 63 medium position of ramp is provided with and the Hydrogen collection chamber
The 64 hydrogen outlet pipes 61 being connected are provided with hydrogen on the hydrogen outlet pipe 61 and go out air cock 62, and the hydrogen goes out
Feed channel 61 is provided with dried pieces 68 with 64 junction of Hydrogen collection chamber, and the 64 downside inner wall of Hydrogen collection chamber is provided with
Lower inclined plane 65,65 medium position of lower inclined plane are provided with the miscellaneous gas outlet pipe 66 being connected with the Hydrogen collection chamber 64,
Miscellaneous gas, which is provided with, on the miscellaneous gas outlet pipe 66 goes out air cock 67；Heat extraction component is provided in described device main body 11, it is described
Heat extraction component includes the annular groove 75 for being arranged on 33 periphery of fan electromotor, is provided with and the fan electromotor in the annular groove 75
The heat dissipating ring 74 of 33 outer surfaces fitting, is provided with the heat emission hole communicated up and down in the heat dissipating ring 74,75 left end of annular groove is set
It is equipped with and air inlet duct 72 is communicated with outside, exhaust fan 71 is installed in the air inlet duct 72,75 right end of annular groove is provided with
With the outgassing groove 73 that communicates of outside, generated heat during so as to be run the fan electromotor 33 by the exhaust fan 71
Discharge, can avoid the accumulation of heat.
Valuably, the first heating chamber 27 is respectively arranged in inner wall before and after the water-gas-vapor reaction chamber 26, it is described
The first resistive heater 28 is provided in first heating chamber 27.
Valuably, the carbon dioxide adsorption chamber 36 is respectively arranged with the second heating in the front and rear inner wall of downside inner wall
Chamber 51 is provided with the second resistive heater 52 in second heating chamber 51.
Valuably, the medium position of the 36 right side inner wall of carbon dioxide adsorption chamber is fixedly installed gas concentration lwevel inspection
Device 38 is surveyed, when gas concentration lwevel reaches designated value in the carbon dioxide adsorption chamber 36, the gas concentration lwevel inspection
Surveying device 38 controls the fan electromotor to rotate, and the gas containing high concentration carbon dioxide in carbon dioxide adsorption chamber 36 is passed through
The carbon dioxide outlet pipe 43 is blown out in specified containers.
The operating process of hydrogen making is carried out by the present apparatus, water-gas air inlet pipe 21 is connected to storage water coal by user of service
On the container of gas, water-gas air inlet switch 22 is opened at this time, water-gas is filled in water-gas-vapor reaction chamber 26, beaten simultaneously
Boiling water steam air inlet switch 24 injects vapor, at this time by vapor air inlet pipe 23 into water-gas-vapor reaction chamber 26
It is powered to the first resistive heater 28 and passes through the first resistive heater 28 and add the temperature in water-gas-vapor reaction chamber 26
For heat to 427 degrees Celsius, the carbon monoxide in the water-gas injected at this time reacts generation with vapor at high operating temperatures
The carbon dioxide and hydrogen of same volume after gas reacts to greatest extent in water-gas-vapor reaction chamber 26, are set to
Pumping fan device 31 on ventilation pipe 32 starts, and the gas in water-gas-vapor reaction chamber 26 is pumped to titanium dioxide
In carbon adsorption chamber 36 and the carbon dioxide adsorption block 41 by being set in outlet pipe 46 is entered in Hydrogen collection chamber 64, this
When the gas that enters in carbon dioxide adsorption chamber 36 include the hydrogen, carbon dioxide and not a small amount of volume of most of volume
The carbon monoxide reacted completely, vapor, when gas passes through carbon dioxide adsorption block 41, the carbon dioxide in gas is by two
Carbonoxide Attraction block 41 is blocked in the carbon dioxide adsorption chamber 36 in 41 left side of carbon dioxide adsorption block, when carbon dioxide adsorption chamber
When gas concentration lwevel in 36 reaches certain value, carbon dioxide concentration detecting device 38 controls fan electromotor 33 to rotate, simultaneously
It is powered to the second resistive heater 52, the carbon dioxide particle in carbon dioxide adsorption chamber 36 is heated to the carbon dioxide suction that comes off
Attached piece 41 and pass through fan blade 35 and enter carbon dioxide blowout carbon dioxide outlet pipe 43 in specified containers, receive at this time
The carbon dioxide collected can be used as the Fertilizer application of booth vegetable, and enter the gas in Hydrogen collection chamber 64 by outlet pipe 46
Body is hydrogen and a small amount of carbon monoxide and vapor, since the relative molecular mass of hydrogen is much smaller than carbon monoxide and vapor
Relative molecular mass, therefore hydrogen floats on upper strata in Hydrogen collection chamber 64, and carbon monoxide and vapor are then deposited on
The bottom of Hydrogen collection chamber 64, opening hydrogen, which goes out air cock 62, at this time to extract the hydrogen in Hydrogen collection chamber 64 out, make
Become more, therefore need to periodically open miscellaneous gas and go out air cock 67 by Hydrogen collection chamber with the miscellaneous gas in Hydrogen collection chamber 64 after the time of one end
Miscellaneous gas in 64 releases to prevent from reducing by the density of hydrogen that the present apparatus is collected.
The beneficial effects of the invention are as follows：The configuration of the present invention is simple, it is easy to operate, the behaviour of hydrogen making is carried out by the present apparatus
Make process, water-gas air inlet pipe is connected on the container of storage water-gas by user of service, and opening water-gas air inlet switch at this time will
Water-gas is filled in water-gas-vapor reaction chamber, opens simultaneously vapor air inlet switch, by vapor air inlet pipe to water coal
Air-water vapor reaction intracavitary injects vapor, is powered at this time to the first resistive heater and passes through the first resistive heater by water
Temperature in coal gas-vapor reaction chamber is heated to 427 degrees Celsius, the carbon monoxide in the water-gas injected at this time
It reacts the carbon dioxide and hydrogen of generation same volume at high operating temperatures with vapor, treats gas in water-gas-vapor reaction chamber
It after body reacts to greatest extent, is set to pumping fan device on ventilation pipe and starts, and by water-gas-vapor reaction chamber
Interior gas pumps to carbon dioxide adsorption intracavitary and the carbon dioxide adsorption block by being set in outlet pipe enters hydrogen
In gas collecting chamber, enter at this time carbon dioxide adsorption intracavitary gas include the hydrogen of most of volume, carbon dioxide with
And the carbon monoxide reacted completely, the vapor of not a small amount of volume, when gas passes through carbon dioxide adsorption block, two in gas
Carbonoxide is blocked in the carbon dioxide adsorption intracavitary on the left of carbon dioxide adsorption block by carbon dioxide adsorption block, when carbon dioxide is inhaled
When the gas concentration lwevel of attached intracavitary reaches certain value, carbon dioxide concentration detecting device control fan electromotor rotation is given simultaneously
Second resistive heater is powered, and is heated to coming off carbon dioxide adsorption block simultaneously by the carbon dioxide particle of carbon dioxide adsorption intracavitary
Carbon dioxide blowout carbon dioxide outlet pipe is entered in specified containers by fan blade, the titanium dioxide being collected at this time
Carbon can be used as the Fertilizer application of booth vegetable, and enter the gas of Hydrogen collection intracavitary for hydrogen and a small amount of by outlet pipe
Carbon monoxide and vapor, since the relative molecular mass of hydrogen is much smaller than the relative molecular mass of carbon monoxide and vapor,
Therefore hydrogen floats on upper strata in Hydrogen collection intracavitary, and carbon monoxide and vapor are then deposited on the bottom of Hydrogen collection chamber,
Opening hydrogen, which goes out air cock, at this time to extract the hydrogen of Hydrogen collection intracavitary out, the Hydrogen collection intracavitary after one end time is used
Miscellaneous gas become more, therefore need to periodically open miscellaneous gas and go out air cock by the releasing of the miscellaneous gas of Hydrogen collection intracavitary to prevent from passing through the present apparatus
The density of hydrogen of collection reduces.
The above description is merely a specific embodiment, but protection scope of the present invention is not limited thereto, any
The change or replacement expected without creative work, should be covered by the protection scope of the present invention.Therefore, it is of the invention
Protection domain should be determined by the scope of protection defined in the claims.
Claims (4)
1. a kind of water-gas hydrogen producer, including apparatus main body, the carbon dioxide adsorption device being set in described device main body,
It is set to the water-gas on the left of described device main body-vapor reaction unit and the hydrogen being set on the right side of described device main body
Collection device, the water-gas-vapor reaction unit include retort, water-gas-vapor are provided in the retort
Reaction chamber, the water-gas-vapor reaction chamber inner left wall is provided with to be connected with the water-gas-vapor reaction chamber
Water-gas air inlet pipe, is provided with water-gas air inlet switch in the water-gas air inlet pipe, on the water-gas-vapor reaction chamber
Side inner wall is provided with the vapor air inlet pipe being connected with the water-gas-vapor reaction chamber, in the vapor air inlet pipe
Vapor air inlet switch is provided with, apparatus main body is provided on the right side of the retort, titanium dioxide is provided in described device main body
Carbon adsorption device, the carbon dioxide adsorption device includes the carbon dioxide adsorption chamber being set in described device main body, described
It is provided between apparatus main body and the retort and connects the water-gas-vapor reaction chamber and the carbon dioxide adsorption chamber
Ventilation pipe, pumping fan device is provided on the ventilation pipe, in the carbon dioxide adsorption chamber upper inside walls fixation set
Fan electromotor is equipped with, the fan electromotor lower end is connected with fan blade, the carbon dioxide adsorption by shaft power
The carbon dioxide outlet pipe being connected with the carbon dioxide adsorption chamber is provided in inner wall on the downside of chamber, the carbon dioxide goes out
Feed channel is provided with ramp structure with the carbon dioxide adsorption chamber connection, is provided on the carbon dioxide outlet pipe
Carbon dioxide goes out air cock, and Hydrogen collection device is provided on the right side of described device main body, and the Hydrogen collection device includes fixing
It is connected in the collection main body of described device main body right end face, described collect in main body is provided with Hydrogen collection chamber, described
Be provided in inner wall on the right side of i.e. described carbon dioxide adsorption chamber in Hydrogen collection chamber inner left wall the connection Hydrogen collection chamber and
The outlet pipe of the carbon dioxide adsorption chamber, the outlet pipe are provided with dioxy with the carbon dioxide adsorption chamber junction
Change carbon adsorption block, the Hydrogen collection chamber upper inside walls are provided with ramp, the ramp medium position be provided with it is described
The hydrogen outlet pipe that Hydrogen collection chamber is connected is provided with hydrogen on the hydrogen outlet pipe and goes out air cock, the hydrogen
Outlet pipe is provided with dried pieces with the Hydrogen collection chamber junction, and Hydrogen collection chamber downside inner wall is provided with oblique
Face, the lower inclined plane medium position are provided with the miscellaneous gas outlet pipe being connected with the Hydrogen collection chamber, the miscellaneous gas outlet
Miscellaneous gas is provided on pipeline and goes out air cock；Heat extraction component is provided in described device main body, the heat extraction component includes being arranged on
The annular groove of the fan electromotor periphery is provided with the heat dissipating ring being bonded with the fan electromotor outer surface in the annular groove, described
The heat emission hole communicated up and down is provided in heat dissipating ring, the annular groove left end is provided with and air inlet duct is communicated with outside, the air inlet duct
In be installed with exhaust fan, the annular groove right end is provided with the outgassing groove communicated with outside, so as to pass through the exhaust fan
Generated heat discharge, can avoid the accumulation of heat when the fan electromotor is run.
2. a kind of water-gas hydrogen producer according to claim 1, it is characterised in that：The water-gas-vapor reaction
The first heating chamber is respectively arranged with before and after chamber in inner wall, the first resistive heater is provided in first heating chamber.
3. a kind of water-gas hydrogen producer according to claim 1, it is characterised in that：The carbon dioxide adsorption chamber is close
The second heating chamber is respectively arranged in the front and rear inner wall of downside inner wall, the second adding thermal resistance is provided in second heating chamber
Silk.
4. a kind of water-gas hydrogen producer according to claim 1, it is characterised in that：On the right side of the carbon dioxide adsorption chamber
The medium position of inner wall is fixedly installed carbon dioxide concentration detecting device, when the carbon dioxide adsorption intracavitary carbon dioxide is dense
When degree reaches designated value, the carbon dioxide concentration detecting device controls the fan electromotor rotation, by carbon dioxide adsorption chamber
The interior gas containing high concentration carbon dioxide is blown out to by the carbon dioxide outlet pipe in specified containers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810119694.9A CN108264020B (en) | 2018-02-06 | 2018-02-06 | A kind of water-gas hydrogen producer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810119694.9A CN108264020B (en) | 2018-02-06 | 2018-02-06 | A kind of water-gas hydrogen producer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN108264020A true CN108264020A (en) | 2018-07-10 |
| CN108264020B CN108264020B (en) | 2019-02-22 |
Family
ID=62773724
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810119694.9A Active CN108264020B (en) | 2018-02-06 | 2018-02-06 | A kind of water-gas hydrogen producer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108264020B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102530862A (en) * | 2012-03-12 | 2012-07-04 | 浠水县福瑞德化工有限责任公司 | Carbon monoxide conversion method for ammonia synthesis |
| CN202575967U (en) * | 2012-04-16 | 2012-12-05 | 洁星环保科技投资（上海）有限公司 | Hydrogen-manufacturing device |
| CN103060003A (en) * | 2012-12-27 | 2013-04-24 | 东南大学 | Method and device for preparing H2 and separating CO2 based on calcium-based sorbent |
| CN203820445U (en) * | 2014-02-26 | 2014-09-10 | 上海合既得动氢机器有限公司 | Small methanol water hydrogen production equipment |
| CN104962316A (en) * | 2015-06-30 | 2015-10-07 | 中国科学院工程热物理研究所 | Grading-gasification moderate-circulation type chemical-power polygeneration system for gathering CO2. |
-
2018
- 2018-02-06 CN CN201810119694.9A patent/CN108264020B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102530862A (en) * | 2012-03-12 | 2012-07-04 | 浠水县福瑞德化工有限责任公司 | Carbon monoxide conversion method for ammonia synthesis |
| CN202575967U (en) * | 2012-04-16 | 2012-12-05 | 洁星环保科技投资（上海）有限公司 | Hydrogen-manufacturing device |
| CN103060003A (en) * | 2012-12-27 | 2013-04-24 | 东南大学 | Method and device for preparing H2 and separating CO2 based on calcium-based sorbent |
| CN203820445U (en) * | 2014-02-26 | 2014-09-10 | 上海合既得动氢机器有限公司 | Small methanol water hydrogen production equipment |
| CN104962316A (en) * | 2015-06-30 | 2015-10-07 | 中国科学院工程热物理研究所 | Grading-gasification moderate-circulation type chemical-power polygeneration system for gathering CO2. |
Also Published As
| Publication number | Publication date |
|---|---|
| CN108264020B (en) | 2019-02-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108658041A (en) | A kind of water-gas hydrogen generating system | |
| CN108036337A (en) | Indoor condensed combustion device | |
| CN108264020B (en) | A kind of water-gas hydrogen producer | |
| CN106524232B (en) | A kind of Multifunctional biomass cauldron kitchen range | |
| CN108313980A (en) | A kind of water-gas device for producing hydrogen | |
| CN110469865B (en) | Boiler waste heat recycling device | |
| CN108148644A (en) | A kind of gas mixed gas purifying plant and its application method based on chemical reaction | |
| CN108128753A (en) | A kind of natural gas hydrogen-preparing device | |
| CN208995439U (en) | For imparting knowledge to students or the biomass pyrolytic of scientific research and the charcoal gas-liquid combined production device of gasification | |
| CN103691139B (en) | Residual heat heating system for evaporator | |
| CN113016983A (en) | Energy-saving type pre-steaming device for can processing and using method | |
| CN107166357B (en) | Double-loop scale-free steam generating device | |
| CN202973067U (en) | Biomass fuel gasified combustion furnace | |
| CN210568323U (en) | Boiler evaporates supplementary device based on air-blower | |
| CN206709132U (en) | A kind of fluid diaphragm side-draft integrated stove | |
| CN206905034U (en) | A kind of Multifunctional biomass cauldron kitchen range | |
| CN110668400A (en) | Biomass hydrogen production and gas washing integrated device | |
| CN206000586U (en) | Circulation electric generating apparatus | |
| CN201068440Y (en) | Biomass gasification furnace | |
| CN208170409U (en) | A kind of heating device of torch liquid separation tank | |
| CN107131490B (en) | Double-loop scale-free steam generation structure | |
| CN209230313U (en) | A kind of belt cooler vent flue gas circulating device in power generation by sintered waste heat | |
| CN2898638Y (en) | Gas generator with water tank | |
| CN211450990U (en) | Clean energy utilization device of thermal power plant | |
| CN210057404U (en) | High-efficient enrichment facility is used in production of cyclobutane class product |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20190109 Address after: 545616 No. 511, Building 2, Guantang Pioneer Park R&D Center, Liudong New District, Liuzhou City, Guangxi Zhuang Autonomous Region Applicant after: LIUZHOU HAOXIANGTE SCIENCE & TECHNOLOGY Co.,Ltd. Address before: 246500 No. 104 Susong North Road, Susong County Industrial Park, Anqing City, Anhui Province Applicant before: Wu Boting |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230331 Address after: No. 51, Liuliku, Jinlian Village (18), Pingwang Town, Wujiang District, Suzhou City, Jiangsu Province, 215000 Patentee after: Zhang Ming Patentee after: Shen Siyuan Address before: 545616 No. 511, Building 2, Guantang Pioneer Park R&D Center, Liudong New District, Liuzhou City, Guangxi Zhuang Autonomous Region Patentee before: LIUZHOU HAOXIANGTE SCIENCE & TECHNOLOGY Co.,Ltd. |