CN207377678U - A kind of schizolysis hydrogen production plant and automobile - Google Patents
A kind of schizolysis hydrogen production plant and automobile Download PDFInfo
- Publication number
- CN207377678U CN207377678U CN201721203601.8U CN201721203601U CN207377678U CN 207377678 U CN207377678 U CN 207377678U CN 201721203601 U CN201721203601 U CN 201721203601U CN 207377678 U CN207377678 U CN 207377678U
- Authority
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- China
- Prior art keywords
- hydrogen production
- cracking
- production plant
- cracking reactor
- schizolysis
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 48
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 48
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 36
- 238000005336 cracking Methods 0.000 claims abstract description 77
- 239000007789 gas Substances 0.000 claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 25
- 238000006243 chemical reaction Methods 0.000 claims abstract description 19
- 238000012546 transfer Methods 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000003054 catalyst Substances 0.000 claims description 11
- 230000008676 import Effects 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 2
- 239000000446 fuel Substances 0.000 claims 1
- 239000002918 waste heat Substances 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 150000002431 hydrogen Chemical class 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 11
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 238000010586 diagram Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000001569 carbon dioxide Substances 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000007086 side reaction Methods 0.000 description 2
- 229910000570 Cupronickel Inorganic materials 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- QVQLCTNNEUAWMS-UHFFFAOYSA-N barium oxide Inorganic materials [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 description 1
- CSSYLTMKCUORDA-UHFFFAOYSA-N barium(2+);oxygen(2-) Chemical compound [O-2].[Ba+2] CSSYLTMKCUORDA-UHFFFAOYSA-N 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- YOCUPQPZWBBYIX-UHFFFAOYSA-N copper nickel Chemical compound [Ni].[Cu] YOCUPQPZWBBYIX-UHFFFAOYSA-N 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 description 1
- 229910001950 potassium oxide Inorganic materials 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance 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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Hydrogen, Water And Hydrids (AREA)
Abstract
The utility model provides a kind of schizolysis hydrogen production plant and automobile, is related to automobile technical field.The schizolysis hydrogen production plant includes cracking reactor, engine, the output of products pipeline for the feedstock transportation pipeline that conveys first alcohol and water and for exporting combustion-supporting hydrogen, material inlet and cracking gas outlet are provided on cracking reactor, material inlet is connected with feedstock transportation pipeline, and cracking gas outlet is connected by output of products pipeline with engine；Cracking reactor includes reaction chamber and the heat transfer space for controlling reaction chamber temperature, waste pipe are connected with heat transfer space.Engine power can be promoted and reduce energy consumption, efficiently use the waste heat of engine, promote the utilization rate of the energy.The utility model additionally provides a kind of automobile, including above-mentioned schizolysis hydrogen production plant, is likewise supplied with above-mentioned advantage.
Description
Technical field
The utility model is related to automobile technical field, in particular to a kind of schizolysis hydrogen production plant and automobile.
Background technology
With the promotion of people's quality of the life, automobile has become the required vehicles of people, while country is to environmental protection
Advocating for energy saving aspect makes automobile progressively tend to the aspect development for reducing energy consumption and environmental pollution.
But the phenomenon that existing automobile is low there is heat utilization rate, and a large amount of waste heats are distributed and wasted.
Utility model content
The purpose of this utility model is to provide a kind of schizolysis hydrogen production plants, it is intended to improve that automobile heat utilization ratio is low to ask
Topic.
The another object of the utility model is to provide a kind of automobile, and energy utilization rate is high, meet it is energy-saving and environment-friendly will
It asks.
The utility model is realized in this way：
A kind of schizolysis hydrogen production plant, including cracking reactor, engine, the feedstock transportation pipeline for conveying first alcohol and water
With for exporting the output of products pipeline of combustion-supporting hydrogen, be provided with material inlet and cracking gas outlet on cracking reactor, raw material into
Mouth is connected with feedstock transportation pipeline, and cracking gas outlet is connected by output of products pipeline with engine；
Cracking reactor includes reaction chamber and the heat transfer space for controlling reaction chamber temperature, waste pipe
It is connected with heat transfer space.
Further, in the utility model preferred embodiment, schizolysis hydrogen production plant further includes accumulator, accumulator
Outlet is connected with feedstock transportation pipeline, and feed line road is provided with pressure regulator valve.
Further, it is additionally provided with to regulate and control letting out for pressure in the utility model preferred embodiment, on accumulator
Pressure valve.
Further, in the utility model preferred embodiment, temperature control device is additionally provided on cracking reactor,
And catalyst for cracking is filled in cracking reactor.
Further, in the utility model preferred embodiment, multiple clothes are provided in the housing of cracking reactor
Plate, each drapery panel extend to housing close to one end that cracking gas exports, Mei Gebu from housing close to one end of material inlet
Catalyst for cracking is distributed on flitch.
Further, in the utility model preferred embodiment, the bottom of cracking reactor is provided with agitating device, stirs
Mixing device includes actuator, agitating shaft and the agitating vane being fixed on agitating shaft, and output shaft and the agitating shaft of actuator are driven
Connection, agitating shaft to be driven to rotate.
Further, in the utility model preferred embodiment, the bottom of housing is provided with collection conduit and collecting tank,
Multiple relief holes are provided on the bottom wall of housing, is formed between collection conduit and agitating device and collects separate space, each relief hole leads to
Collection separate space is crossed to connect with collecting tank.
Further, in the utility model preferred embodiment, be provided on the bottom wall of collecting tank material taking mouth and with
The bottom wall of the matched feeding cover board of material taking mouth, feeding cover board and collecting tank is detachably connected.
A kind of automobile, including afterbody oil supply system and above-mentioned schizolysis hydrogen production plant, afterbody oil supply system and cracking reactor
It is connected.
Further, in the utility model preferred embodiment, when schizolysis hydrogen production plant has accumulator, accumulator
Outlet is connected with feedstock transportation pipeline, and the import of accumulator is connected by pipeline road with afterbody oil supply system.
The beneficial effects of the utility model are：The schizolysis hydrogen production plant that the utility model is obtained by above-mentioned design leads to
It crosses and the reaction raw materials that first alcohol and water forms is delivered in cracking reactor, and hydrogen product after the completion of cracking etc. is delivered to
Engine combustion-supporting does work, and promotes engine power and reduces energy consumption；The heat transfer space of waste pipe and cracking reactor
The waste heat of engine can be utilized by being connected in catalytic process, promote the utilization rate of the energy.The utility model additionally provides one kind
Automobile including above-mentioned schizolysis hydrogen production plant, is likewise supplied with above-mentioned advantage.
Description of the drawings
It, below will be to required in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment
The attached drawing used is briefly described, it should be understood that and the following drawings illustrates only some embodiments of the utility model, therefore not
The restriction to scope is should be considered as, for those of ordinary skill in the art, without creative efforts,
It can also be obtained according to these attached drawings other relevant attached drawings.
Fig. 1 is the structure diagram for the schizolysis hydrogen production plant that the utility model first embodiment provides；
Fig. 2 is the structure diagram for the cracking reactor that the utility model second embodiment provides；
Fig. 3 is the bottom substance schematic diagram of collecting tank in Fig. 2；
Fig. 4 is the structure diagram for the feeding cover board that the utility model second embodiment provides；
Fig. 5 is the structure diagram of fastener in Fig. 4；
Fig. 6 is the structure diagram for the automobile that the utility model embodiment provides.
Icon：100a- schizolysis hydrogen production plants；110- cracking reactors；111- temperature control devices；112- material inlets；
113- drapery panels；114- cracking gases export；115- agitating devices；1152- actuators；1154- agitating shafts；1156- agitating vanes；
116- reaction chambers；117- gas vents；118- heat transfer spaces；119- relief holes；1191- fasteners；1192- collects separate space；
1194- collection conduits；1195- breaks part into two with one's hands；1196- collecting tanks；1198- material taking mouths；1199- feeding cover boards；120- engines；
122- exhaust pipes；130- feedstock transportation pipelines；132- pressure regulator valves；140- output of products pipelines；150- accumulators；152- pressure releases
Valve；160- afterbody oil supply systems.
Specific embodiment
To make the purpose, technical scheme and advantage of the utility model embodiment clearer, below in conjunction with this practicality
The technical solution in the utility model embodiment is clearly and completely described in attached drawing in new embodiment, shows
So, described embodiment is the embodiment of a part of embodiment of the utility model rather than whole.Based on this practicality
Embodiment in new, those of ordinary skill in the art are obtained every other without creative efforts
Embodiment shall fall within the protection scope of the present invention.Therefore, the implementation to the utility model provided in the accompanying drawings below
The detailed description of mode is not intended to limit claimed the scope of the utility model, but is merely representative of the utility model
Selected embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not making creative labor
The every other embodiment obtained under the premise of dynamic, shall fall within the protection scope of the present invention.
In the description of the utility model, it is to be understood that term " length ", " width ", " thickness ", " on ", " under ",
The orientation or position relationship of the instructions such as "front", "rear", "left", "right", " vertical ", " level ", " top ", " bottom ", " interior ", " outer " are
Based on orientation shown in the drawings or position relationship, it is for only for ease of description the utility model and simplifies description rather than instruction
Or imply that signified equipment or element must have specific orientation, with specific azimuth configuration and operation, therefore be not understood that
For the limitation to the utility model.
In addition, term " first ", " second " are only used for description purpose, and it is not intended that instruction or hint relative importance
Or the implicit quantity for indicating indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Implicitly include one or more this feature.In the description of the utility model, " multiple " are meant that two or two
More than, unless otherwise specifically defined.
In the utility model, unless otherwise clearly defined and limited, term " installation ", " connected ", " connection ", " Gu
It is fixed " etc. terms should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected or integral；Can be
Mechanical connection or electrical connection；It can be directly connected, can also be indirectly connected by intermediary, can be two
The interaction relationship of connection or two elements inside element.It for the ordinary skill in the art, can basis
Concrete condition understands concrete meaning of the above-mentioned term in the utility model.
In the utility model, unless otherwise clearly defined and limited, fisrt feature second feature it " on " or it
" under " can be contacted directly including the first and second features, it is not to contact directly but lead to that can also include the first and second features
Cross the other characterisation contact between them.Moreover, fisrt feature second feature " on ", " top " and " above " include the
One feature is directly over second feature and oblique upper or is merely representative of fisrt feature level height higher than second feature.First is special
Sign second feature " under ", " lower section " and " below " including fisrt feature immediately below second feature and obliquely downward or only
Represent that fisrt feature level height is less than second feature.
First embodiment
Fig. 1 is refer to, the utility model embodiment provides a kind of schizolysis hydrogen production plant 100a, including cracking reactor
110th, engine 120, the output of products pipeline for the feedstock transportation pipeline 130 that conveys first alcohol and water and for exporting combustion-supporting hydrogen
140, material inlet 112 and cracking gas outlet 114, material inlet 112 and feedstock transportation pipeline are provided on cracking reactor 110
130 connections, cracking gas outlet 114 are connected by output of products pipeline 140 with engine 120；Cracking reactor 110 includes reaction
Chamber 116 and the heat transfer space 118 for controlling 116 temperature of reaction chamber, the exhaust pipe 122 and heat transfer space of engine 120
118 are connected.
It should be noted that first alcohol and water is delivered in cracking reactor 110 by feedstock transportation pipeline 130 crack instead
Should generate cracking gas include carbon dioxide and hydrogen, by output of products pipeline 140 by cracking gas be delivered to engine 120 into
In gas branch pipe, hydrogen can be 120 combustion-supporting acting of engine, can be obviously improved 120 power of engine and reduce oil consumption, energy saving
Rate is in 20-35%.In addition, the exhaust pipe 122 of engine 120 is connected with the heat transfer space 118 of cracking reactor 110, splitting
It can be heated up in solution preocess using the waste heat of engine 120, promote reaction rate and energy utilization rate, be more in line with energy saving
The requirement of environmental protection.
Methanol and the equation of water-splitting reaction are specifically introduced.(1) main reaction equation：CH3OH=CO+2H2(+
90.7KJ/mol)；CO+H2O=CO2+H2(-41.2KJ/mol).(2) overall reaction equation：CH3OH+H2O=CO2+3H2(+
49.5KJ/mol).(3) side reaction equation：2CH3OH=CH3OCH3+H2O(-24.9KJ/mol)；CO+3H2=CH4+H2O(-
206.3KJ/mol)。
Specifically, the caliber of feedstock transportation pipeline 130 and output of products pipeline 140 is unlimited, can be according to specific technique
It is required that it is set.The concrete structure of engine 120 is unlimited, can be the power-equipment of the devices such as existing automobile.
Further, schizolysis hydrogen production plant 100a further includes accumulator 150, the outlet of accumulator 150 and feed line
Road 130 connects, and pressure regulator valve 132 is provided on feedstock transportation pipeline 130.Accumulator 150 is for original of the storage containing first alcohol and water
Material, can come from other devices can also artificially add in.
Specifically, pressure regulator valve 132 can be pin type pressure regulator valve, can be with the flow of accuracy controlling raw material, and can control will adjust
Pressure valve 132 is connected with controller, is facilitated the aperture of control pressure regulator valve 132 and then is controlled the flow velocity and flow of raw material.Accumulator 150
Can be general bucket body structure, volume substantially 2L.
Further, it is additionally provided with to regulate and control the relief valve 152 of pressure on accumulator 150.Pressure in accumulator 150
Power can carry out row pressure when excessively high by relief valve 152, to enhance the security in operating process.
Further, temperature control device 111, and filling in cracking reactor 110 are additionally provided on cracking reactor 110
There is catalyst for cracking.The heating element of temperature control device 111 is located in heat transfer space 118, can to cracking reactor 110 into
Row heating.Specifically, temperature control device 111 can be connected by circuit with power supply, make temperature control device 111 by electric energy
Heating element heating, and then the gas heating in heat transfer space 118 is driven to regulate and control the reaction chamber of cracking reactor 110
116 temperature.120 temperature of engine is not high when just starting to start, and first opening temperature regulation device 111 exchanges heat space 118
Interior gas heats up.
Further, the temperature in cracking reactor 110 is 200-500 DEG C, is preferably 250-350 DEG C.To promote to react
The conversion ratio of hydrogen and rate of side reactions is reduced to a certain extent, temperature need to control within the specific limits in the process.In this temperature
In the range of pyrolysis product be 74% hydrogen and 24% carbon dioxide, it is energy saving reach 20-35%.
Second embodiment
The technique effect of the device that the utility model embodiment is provided, realization principle and generation and first embodiment phase
Together, to briefly describe, the present embodiment does not refer to part, corresponding contents in first embodiment is can refer to, the difference is that this reality
Apply the structure of cracking reactor 110 in example.
Further, Fig. 2 is refer to, multiple drapery panels 113, each cloth are provided in the housing of cracking reactor 110
Plate 113 extends to housing close to one end of cracking gas outlet 114, each cloth from housing close to one end of material inlet 112
Catalyst for cracking is distributed on plate 113.Drapery panel 113 can promote the uniformity of feed distribution, can be on drapery panel 113
Tiny through-hole structure is set, and the diameter of through hole is slightly less than the size of catalyst, so that catalyst is distributed on drapery panel 113
Gas can be flowed by through hole.
Specifically, catalyst can be common methanol cracking catalyst, such as copper-nickel catalyst cooperation potassium oxide, calcium oxide
Or the auxiliary agents such as barium monoxide.
Further, the bottom of cracking reactor 110 is provided with agitating device 115, and agitating device 115 includes actuator
1152nd, agitating shaft 1154 and the agitating vane 1156 being fixed on agitating shaft 1154, the output shaft and agitating shaft of actuator 1152
1154 are sequentially connected, agitating shaft 1154 to be driven to rotate.Set agitating device 115 can be right in the bottom of cracking reactor 110
It reacts the liquid generated or solid-state like material is stirred, uncracked complete material is promoted to continue to crack, is also promoted simultaneously
The flowing of gas has certain effect for promoting reaction rate.
In addition, multiple gas vents 117 are additionally provided on cracking reactor 110, the gas pressure in cracking reactor 110
Power can be discharged portion gas by gas vent 117 when excessive, promote the safety coefficient of operation.
Further, incorporated by reference to Fig. 2-Fig. 5, the bottom of housing is provided with collection conduit 1194 and collecting tank 1196, housing
Bottom wall on be provided with multiple relief holes 119, between collection conduit 1194 and agitating device 115 formed collect separate space 1192, often
A relief hole 119 is connected by collecting separate space 1192 with collecting tank 1196.When cracking completion liquid object has been retained in reactor
Liquid can be expelled in collecting tank 1196, so as to the progress of follow-up cracking process by matter by relief hole 119.
Further, be provided on the bottom wall of collecting tank 1196 material taking mouth 1198 and with material taking mouth 1198 is matched takes
Expect cover board 1199, feeding cover board 1199 and the bottom wall of collecting tank 1196 are detachably connected.It can be by removing feeding cover board 1199
The outflow of liquid is controlled, residual liquid material is discharged.
It is adapted in the size and the size of feeding cover board 1199 of the material taking mouth 1198 of the bottom of collecting tank 1196.In feeding
Fastener 1191 is provided on cover board 1199 and breaks part 1195 into two with one's hands.It can be quickly by fastener 1191 from taking by breaking part 1195 into two with one's hands
The discharge for carrying out material again is removed in material mouth 1198.Fastener 1191 has the structure of bending as shown in FIG., so as to preferably
It is connected with collecting tank 1196.
It should be noted that in the heat transfer space 118 and first embodiment of the cracking reactor 110 provided in the present embodiment
Structure it is roughly the same.
Fig. 6 is refer to, a kind of utility model embodiment additionally provides a kind of automobile, including afterbody oil supply system 160 and upper
Schizolysis hydrogen production plant 100a is stated, afterbody oil supply system 160 is connected with cracking reactor 110.
Specifically, when schizolysis hydrogen production plant 100a has accumulator 150, outlet and the feedstock transportation pipeline of accumulator 150
130 connections, the import of accumulator 150 are connected by pipeline road with afterbody oil supply system 160.The afterbody of automobile tail is supplied
Feedstock oil in oil system 160 is delivered in accumulator 150, and entire automobile forms a cracking hydrogen production system, improves raw material
Utilization rate and capacity usage ratio.
Specifically, the components such as the oil supply line in afterbody oil supply system 160, delivery pump, liquid level signal line and existing dress
The structure and operation principle put are roughly the same, do not do excessively repeating herein.
In conclusion the utility model provides a kind of schizolysis hydrogen production plant, by feedstock transportation pipeline by methanol and
Water, which is delivered to progress cracking reaction generation cracking gas in cracking reactor, includes carbon dioxide and hydrogen, passes through output of products pipeline
Cracking gas is delivered in the air intake branch of engine, hydrogen can be that engine combustion-supporting does work, and can be obviously improved engine
Power simultaneously reduces oil consumption, and fractional energy savings is in 20-35%；Waste pipe is connected with the heat transfer space of cracking reactor,
It can be heated up in cracking process using the waste heat of engine, promote reaction rate and energy utilization rate, be more in line with energy saving
The requirement of environmental protection.
A kind of method of cracking hydrogen production provided by the utility model, it is roughly the same with above-mentioned schizolysis hydrogen production plant, on the one hand
Using the hydrogen that cracking generates to engine combustion-supporting, energy consumption is reduced；On the other hand the waste heat of engine is delivered to cracking
Reactor carries out the heating of reaction gas.
A kind of automobile that utility model provides, including afterbody oil supply system and above-mentioned schizolysis hydrogen production plant, entire automobile-shaped
Into a cracking hydrogen production system, raw material availability and capacity usage ratio are improved.
Above description is merely a prefered embodiment of the utility model, is not intended to limit the utility model, for
For those skilled in the art, various modifications and changes may be made to the present invention.It is all in the spiritual and former of the utility model
Within then, any modifications, equivalent replacements and improvements are made should be included within the scope of protection of this utility model.
Claims (10)
1. a kind of schizolysis hydrogen production plant, which is characterized in that including cracking reactor, engine, the original for conveying first alcohol and water
Material conveying tube road and the output of products pipeline for exporting combustion-supporting hydrogen are provided with material inlet and cracking on the cracking reactor
Gas exports, and the material inlet is connected with the feedstock transportation pipeline, and the cracking gas outlet passes through the output of products pipeline
It is connected with the engine；
The cracking reactor includes reaction chamber and the heat transfer space for controlling the reaction chamber temperature, the engine
Exhaust pipe be connected with the heat transfer space.
2. schizolysis hydrogen production plant according to claim 1, which is characterized in that the schizolysis hydrogen production plant further includes storing
Device, the outlet of the accumulator are connected with the feedstock transportation pipeline, and the feed line road is provided with pressure regulator valve.
3. schizolysis hydrogen production plant according to claim 2, which is characterized in that be additionally provided with to regulate and control on the accumulator
The relief valve of pressure.
4. schizolysis hydrogen production plant according to claim 1, which is characterized in that be additionally provided with temperature on the cracking reactor
Regulation device, and it is filled with catalyst for cracking in the cracking reactor.
5. schizolysis hydrogen production plant according to claim 4, which is characterized in that be provided in the housing of the cracking reactor
Multiple drapery panels, it is close that each drapery panel from the housing extends to the housing close to one end of the material inlet
One end of the cracking gas outlet, is each distributed with catalyst for cracking on the drapery panel.
6. schizolysis hydrogen production plant according to claim 5, which is characterized in that the bottom of the cracking reactor, which is provided with, to be stirred
Device is mixed, the agitating device includes actuator, agitating shaft and the agitating vane being fixed on the agitating shaft, the actuator
Output shaft and the agitating shaft be sequentially connected, the agitating shaft to be driven to rotate.
7. schizolysis hydrogen production plant according to claim 6, which is characterized in that the bottom of the housing is provided with collection conduit
And collecting tank, multiple relief holes are provided on the bottom wall of the housing, are formed between the collection conduit and the agitating device
Separate space is collected, each relief hole is connected by the collection separate space with the collecting tank.
8. schizolysis hydrogen production plant according to claim 7, which is characterized in that be provided with and take on the bottom wall of the collecting tank
Material mouth and with the matched feeding cover board of the material taking mouth, the bottom wall of the feeding cover board and the collecting tank is detachably connected.
9. a kind of automobile, which is characterized in that including the cracking hydrogen production any one of afterbody oil supply system and claim 1-8
Device, the afterbody oil supply system are connected with the cracking reactor.
10. automobile according to claim 9, which is characterized in that when the schizolysis hydrogen production plant has accumulator, the storage
The outlet of glassware is connected with the feedstock transportation pipeline, and the import of the accumulator passes through pipeline road and the afterbody fuel feeding system
System is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721203601.8U CN207377678U (en) | 2017-09-19 | 2017-09-19 | A kind of schizolysis hydrogen production plant and automobile |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721203601.8U CN207377678U (en) | 2017-09-19 | 2017-09-19 | A kind of schizolysis hydrogen production plant and automobile |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207377678U true CN207377678U (en) | 2018-05-18 |
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ID=62341040
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721203601.8U Active CN207377678U (en) | 2017-09-19 | 2017-09-19 | A kind of schizolysis hydrogen production plant and automobile |
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| Country | Link |
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| CN (1) | CN207377678U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107476880A (en) * | 2017-09-19 | 2017-12-15 | 重庆润泰节能科技有限公司 | The method, apparatus and automobile of a kind of cracking hydrogen production |
-
2017
- 2017-09-19 CN CN201721203601.8U patent/CN207377678U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107476880A (en) * | 2017-09-19 | 2017-12-15 | 重庆润泰节能科技有限公司 | The method, apparatus and automobile of a kind of cracking hydrogen production |
| CN107476880B (en) * | 2017-09-19 | 2024-04-26 | 重庆大义能源有限公司 | Method and device for producing hydrogen by pyrolysis and automobile |
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