CN106015926A - Compressed hydrogen storage and charging system of hydrogen refueling station - Google Patents
Compressed hydrogen storage and charging system of hydrogen refueling station Download PDFInfo
- Publication number
- CN106015926A CN106015926A CN201610547222.4A CN201610547222A CN106015926A CN 106015926 A CN106015926 A CN 106015926A CN 201610547222 A CN201610547222 A CN 201610547222A CN 106015926 A CN106015926 A CN 106015926A
- Authority
- CN
- China
- Prior art keywords
- pressure
- pressure gas
- gas
- pipeline
- gas storage
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 48
- 239000001257 hydrogen Substances 0.000 title claims abstract description 46
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 46
- 239000007789 gas Substances 0.000 claims abstract description 171
- 238000005984 hydrogenation reaction Methods 0.000 claims description 23
- 238000007906 compression Methods 0.000 claims description 18
- 230000001105 regulatory Effects 0.000 claims description 9
- 238000003825 pressing Methods 0.000 claims description 2
- 239000000446 fuel Substances 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000001514 detection method Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000036772 blood pressure Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
- F17C5/06—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with compressed gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
- F17C13/025—Special adaptations of indicating, measuring, or monitoring equipment having the pressure as the parameter
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/04—Methods for emptying or filling
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/03—Control means
- F17C2250/032—Control means using computers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0404—Parameters indicated or measured
- F17C2250/043—Pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/0626—Pressure
-
- 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
- Y02E60/32—Hydrogen storage
Abstract
The invention proposes a compressed hydrogen storage and charging system of a hydrogen refueling station. A compressor is respectively connected with a high-pressure gas storage cylinder, a medium-pressure gas storage cylinder, a low-pressure gas storage cylinder and a direct charging pipeline by control valve pipelines; the high-pressure gas storage cylinder, the medium-pressure gas storage cylinder and the low-pressure gas storage cylinder are respectively connected with a high-pressure gas charging pipeline, a medium-pressure gas charging pipeline and a low-pressure gas charging pipeline by pipelines, and are all connected with a release pipeline by pipelines; a gas inlet side pipeline of the release pipeline is connected with a control valve; pipelines on gas intake sides of the high-pressure gas storage cylinder, the medium-pressure gas storage cylinder and the low-pressure gas storage cylinder are all connected with pressure sensors; and a data controller is in signal connection with the pressure sensors and the compressor. The system has the following beneficial effects: the system not only can charge vehicle-mounted gas storage cylinders of hydrogen fuel vehicles through the gas storage cylinder set, but also can directly charge the vehicle-mounted gas storage cylinders of the hydrogen fuel vehicles so as to realize intelligent control of compressed hydrogen storage and charging of the hydrogen refueling station.
Description
Technical field
The present invention relates to hydrogenation stations hydrogen gas storage technology field, particularly relate to a kind of hydrogenation stations hydrogen compression gas storage, gas charging system.
Background technology
The hydrogen fuel cell work process of hydrogen powered vehicle can realize zero-emission, and there is not hydrogen gas leakage problem, with electric motor car lithium
Battery is compared, and performance is more stable, safety.Vehicular hydrogen high pressure tank technology is the most ripe, and safety is high.Hydrogen fuel vapour
The hydrogen filling time of car is suitable with the petrol and diesel oil car oil filling time, and the course continuation mileage of hydrogen powered vehicle can reach 500 public affairs
More than in, the about twice of electric motor car.The hydrogen filling of hydrogen powered vehicle needs to carry out in hydrogenation stations, and domestic demands are progressively built
The vertical distributed network perfecting hydrogenation stations.Pressure in hydrogenation stations hydrogen storage system is up to 70MPa, typically divides high pressure, middle pressure and low
Pressure gas bomb group.When gas bomb group is inflated to car bottle, first it is the inflation of low pressure gas bomb group, followed by middle pressure inflation, be finally
High-pressure aerated.During compressor is to gas bomb group QI invigorating, first gives high-pressure gas cylinder QI invigorating, then give middle pressure bottle group,
After be low pressure bottle group.When being in upward adverse flow of QI peak, it will usually occur that the tolerance in gas bomb group is not enough, be difficult within a short period of time
The phenomenon being full of in time to the vehicle-mounted gas bomb of hydrogen powered vehicle.
Summary of the invention
It is an object of the invention to provide a kind of hydrogenation stations hydrogen compression gas storage, gas charging system, to realize both having passed through gas bomb
Group is inflated to the vehicle-mounted gas bomb of hydrogen powered vehicle and can be inflated directly to the vehicle-mounted gas bomb of hydrogen powered vehicle by compressor again.
The present invention provides a kind of hydrogenation stations hydrogen compression gas storage, gas charging system, including compressor, control valve, high-pressure gas cylinder,
Middle pressure gas bomb, low pressure gas bomb, pressure transducer and recording controller, compressor connects high pressure storage through control valve pipeline respectively
Gas cylinder, middle pressure gas bomb, low pressure gas bomb and directly fill pipeline, high-pressure gas cylinder, middle pressure gas bomb and low pressure gas bomb warp respectively
Pipeline connects high-pressure aerated pipeline, middle pressure inflation line and low inflation pipeline, high-pressure gas cylinder, middle pressure gas bomb and low pressure storage
Gas cylinder connects bleed off pipeline the most by the road, and the air inlet side pipeline of bleed off pipeline connects has control valve, in high-pressure gas cylinder, middle pressure
Be all connected with pressure transducer on the pipeline of gas bomb and low pressure gas bomb air inlet side, recording controller signal connect pressure transducer and
Compressor.
Further, recording controller signal connects control valve.
Further, also including that pressure distributes regulating box, the assembling of described control valve is installed on pressure distribution regulating box.
Further, described control valve is pneumatic operated valve.
Further, described recording controller is programmable logic controller (PLC).
Further, described recording controller is intelligent mobile terminal.
Further, described recording controller connects pressure transducer through Bluetooth signal.
Further, described recording controller connects compressor through Bluetooth signal.
Compared with prior art, the hydrogenation stations hydrogen compression gas storage of the present invention, gas charging system have the characteristics that and advantage:
1, hydrogenation stations hydrogen compression gas storage, the gas charging system of the present invention, both can be by vehicle-mounted to hydrogen powered vehicle of gas bomb group
Gas bomb inflation can be inflated directly to the vehicle-mounted gas bomb of hydrogen powered vehicle by compressor again；
2, hydrogenation stations hydrogen compression gas storage, the gas charging system of the present invention, it is achieved hydrogenation stations hydrogen is compressed gas storage, the intelligence of inflation
Control.
After reading in conjunction with the accompanying the detailed description of the invention of the present invention, the features and advantages of the invention will become clearer from.
Accompanying drawing explanation
In order to be illustrated more clearly that the embodiment of the present invention or technical scheme of the prior art, below will be to embodiment or prior art
In description, the required accompanying drawing used is briefly described, it should be apparent that, the accompanying drawing in describing below is some realities of the present invention
Execute example, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to according to these accompanying drawings
Obtain other accompanying drawing.
Fig. 1 is hydrogenation stations hydrogen compression gas storage, gas charging system structural representation in the embodiment of the present invention；
Wherein,
1, recording controller, 2, compressor, 3, pneumatic operated valve, 4, pressure distribution regulating box, 5, pressure transducer, 61, high
Pressure gas bomb, 62, middle pressure gas bomb, 63, low pressure gas bomb, 71, high-pressure aerated pipeline, 72, middle pressure inflation line, 73,
Low inflation pipeline, 74, directly fill pipeline, 75, bleed off pipeline, 8, vehicle-mounted gas bomb.
Detailed description of the invention
Embodiment 1
As it is shown in figure 1, the present embodiment provides a kind of hydrogenation stations hydrogen compression gas storage, gas charging system, including compressor 2, gas system
Valve 3, pressure distribution regulating box 4, high-pressure gas cylinder 61, middle pressure gas bomb 62, low pressure gas bomb 63, pressure transducer 5 and
Recording controller 1, compressor 2 connects high-pressure gas cylinder 61, middle pressure gas bomb 62, low pressure gas storage through pneumatic operated valve 3 pipeline respectively
Bottle 63 and directly fill pipeline 74, high-pressure gas cylinder 61, middle pressure gas bomb 62 and low pressure gas bomb 63 connect high pressure the most by the road
Inflation line 71, middle pressure inflation line 72 and low inflation pipeline 73, high-pressure gas cylinder 61, middle pressure gas bomb 62 and low pressure
Gas bomb 63 connects bleed off pipeline 75 the most by the road, and the air inlet side pipeline of bleed off pipeline 75 connects has pneumatic operated valve 3, at high pressure
It is all connected with pressure transducer 5, data control on the pipeline of the air inlet side of gas bomb 61, middle pressure gas bomb 62 and low pressure gas bomb 63
Device 1 signal processed connects pressure transducer 5, pneumatic operated valve 3 and compressor 2.Pneumatic operated valve 3 assembling is installed on pressure distribution regulating box 4
On, it is simple to concentrate observation, maintenance pneumatic operated valve 3.
Recording controller 1 can be through pressure transducer 5 detection and high-pressure gas cylinder 61, middle pressure gas bomb 62 and low pressure gas bomb
63 are connected the pressure in pipeline, and are carried out logical judgment by recording controller 1 and control the start and stop of compressor 2, decide whether out
Open compressor 2 and carry out QI invigorating or QI invigorating terminates to close down compressor 2.Compressor 2 gives high-pressure gas cylinder 61, middle pressure gas bomb 62 and
During low pressure gas bomb 63 QI invigorating, control through excess pressure distribution regulating box 4, controlled to open by recording controller 1 successively and store up with high pressure
The pneumatic operated valve 3 that gas cylinder 61 pipeline connects inflates to high-pressure gas cylinder 61, recording controller 1 control to open and middle pressure gas bomb
The pneumatic operated valve 3 that 62 pipelines connect inflates to middle pressure gas bomb 62, recording controller 1 control to open and manage with low pressure gas bomb 63
The pneumatic operated valve 3 that road connects inflates to low pressure gas bomb 63.When there being hydrogen powered vehicle to need to be flushed with hydrogen gas, successively by with low pressure gas storage
Low inflation pipeline 73, middle pressure gas tube 72 and the high pressure that bottle 63, middle pressure gas bomb 62 and high-pressure gas cylinder 61 pipeline connect
Inflation line 71 inflates to vehicle-mounted gas bomb 8.Using gas peak period, when amounts of hydrogen deficiency in high-pressure gas cylinder 61,
Although compressor 2 has been switched on, but still can not meet through high-pressure gas cylinder 61 within a short period of time through high-pressure aerated pipeline 71 to
Vehicle-mounted gas bomb 8 is full of gas, recording controller 1 control and directly fill the pneumatic operated valve 3 that pipeline 74 is connected and open, making by compressor
2 through directly fill pipeline 74 directly to vehicle-mounted gas bomb 8 continue inflation, with save be flushed with hydrogen the gas time.After vehicle-mounted gas bomb 8 is full of
The pneumatic operated valve 3 being connected with high-pressure gas cylinder 61 by recording controller 1 switching control again is opened, and inflates to high-pressure gas cylinder 61.
When recording controller 1 is appointed in pressure transducer 5 detects high-pressure gas cylinder 61, middle pressure gas bomb 62 and low pressure gas bomb 63
When the pressure of one gas bomb exceedes safety value, recording controller 1 controls bleeder pipe by the pneumatic operated valve 3 being connected with bleed off pipeline 75
Line 75 discharging decompressing.
Recording controller 1 is in pressure transducer 5 detects high-pressure gas cylinder 61, middle pressure gas bomb 62 and low pressure gas bomb 63
Less than setting value, (high-pressure gas cylinder 61 setting value is 680bar to the pressure on any road, and middle pressure gas bomb 62 setting value is
550bar, low pressure gas bomb 63 setting value is 400bar) time, compressor 2 all can start.After compressor 2 starts, by pressing
Power distribution regulating box 4 controls, and first gives and detected that pressure was less than setting value Na mono-road pipeline and gas bomb inflation, when this at that time
When the pressure of one road bottle group reaches 710bar (gas cylinder fill-up pressure), compressor 2 can successively detection high-pressure gas cylinder 61, in
Pressure gas bomb 62 and the pressure of low pressure gas bomb 63, the pressure on Ruo Zheji road has less than 705bar (the full rear normal blood pressure lowering of gas cylinder
In the range of pressure), compressor 2 Hui Geigai road gas bomb inflate, when this road gas bomb is full of gas, i.e. pressure reaches 710bar
After, it is switched to next pipeline and gas bomb carries out pressure detecting judgement and inflation.Until recording controller 1 detects high-pressure gas
The pressure of bottle 61, middle pressure gas bomb 62 and low pressure gas bomb 63 is all higher than 705bar, is considered as gas bomb and all fills with gas, pressure
Contracting machine 2 is shut down.
Embodiment 2
The present embodiment is in place of the difference of embodiment 1, and recording controller 1 is programmable logic controller (PLC), FPGA
Controller reliability is high, capacity of resisting disturbance is strong, can stablize, control efficiently the gas storage operation of hydrogen compression gas storage system.Number
Can also be intelligent mobile terminal, such as smart mobile phone according to controller 1, recording controller 1 through Bluetooth signal connect pneumatic operated valve 3,
Pressure transducer 5 and compressor 2, control pneumatic operated valve 3 and the opening and closing of compressor 2, data by recording controller 1
Controller 1 monitors the pressure of each gas bomb through pressure transducer 5, it is achieved to the compression gas storage of hydrogenation stations hydrogen, the intelligence control of inflation
System.In addition, it is omitted pneumatic operated valve 3, pressure transducer 5, compressor 2 are connected with recording controller 1 signal cable,
Facilitate pneumatic operated valve 3, the installation of pressure transducer 5, and the most safe and reliable by Bluetooth transmission at the periphery of hydrogen pipeline.
Certainly, described above is not limitation of the present invention, and the present invention is also not limited to the example above, the art
Change that technical staff is made in the essential scope of the present invention, retrofit, add or replace, also should belong to the protection of the present invention
Scope.
Claims (8)
1. a hydrogenation stations hydrogen compression gas storage, gas charging system, it is characterised in that: include compressor, control valve, high-pressure gas
Bottle, middle pressure gas bomb, low pressure gas bomb, pressure transducer and recording controller, compressor connects height through control valve pipeline respectively
Pressing gas bomb, middle pressure gas bomb, low pressure gas bomb and directly fill pipeline, high-pressure gas cylinder, middle pressure gas bomb and low pressure gas bomb divide
Connect high-pressure aerated pipeline, middle pressure inflation line and low inflation pipeline the most by the road, high-pressure gas cylinder, middle pressure gas bomb and low
Pressure gas bomb connects bleed off pipeline the most by the road, on the air inlet side pipeline of bleed off pipeline connection have control valve, high-pressure gas cylinder,
Being all connected with pressure transducer on the pipeline of middle pressure gas bomb and low pressure gas bomb air inlet side, recording controller signal connects pressure sensing
Device and compressor.
Hydrogenation stations hydrogen the most according to claim 1 compression gas storage, gas charging system, it is characterised in that: recording controller is believed
Number connect control valve.
Hydrogenation stations hydrogen the most according to claim 2 compression gas storage, gas charging system, it is characterised in that: also include that pressure divides
Joining regulating box, the assembling of described control valve is installed on pressure distribution regulating box.
Hydrogenation stations hydrogen the most according to claim 3 compression gas storage, gas charging system, it is characterised in that: described control valve is
Pneumatic operated valve.
Hydrogenation stations hydrogen the most according to claim 4 compression gas storage, gas charging system, it is characterised in that: described Data Control
Device is programmable logic controller (PLC).
Hydrogenation stations hydrogen the most according to claim 4 compression gas storage, gas charging system, it is characterised in that: described Data Control
Device is intelligent mobile terminal.
7. compress gas storage, gas charging system according to the hydrogenation stations hydrogen described in claim 5 or 6, it is characterised in that: described data
Controller connects pressure transducer through Bluetooth signal.
Hydrogenation stations hydrogen the most according to claim 7 compression gas storage, gas charging system, it is characterised in that: described Data Control
Device connects compressor through Bluetooth signal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610547222.4A CN106015926A (en) | 2016-07-12 | 2016-07-12 | Compressed hydrogen storage and charging system of hydrogen refueling station |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610547222.4A CN106015926A (en) | 2016-07-12 | 2016-07-12 | Compressed hydrogen storage and charging system of hydrogen refueling station |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106015926A true CN106015926A (en) | 2016-10-12 |
Family
ID=57109633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610547222.4A Pending CN106015926A (en) | 2016-07-12 | 2016-07-12 | Compressed hydrogen storage and charging system of hydrogen refueling station |
Country Status (1)
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108613012A (en) * | 2016-12-09 | 2018-10-02 | 中国石油化工股份有限公司 | A kind of hydrogenation stations pneumatic type hydrogen compression gas storage system |
| CN109212247A (en) * | 2017-06-30 | 2019-01-15 | 深圳迈瑞生物医疗电子股份有限公司 | The feed liquid method of liquid feed device, sample analyser and liquid feed device |
| CN109210370A (en) * | 2018-09-18 | 2019-01-15 | 北京久安通氢能科技有限公司 | A kind of hydrogenation stations and hydrogenation control method |
| CN109237296A (en) * | 2018-09-21 | 2019-01-18 | 浙江昊凡科技有限公司 | A kind of hydrogen supply method and system applied to hydrogenation stations |
| CN110939860A (en) * | 2018-09-21 | 2020-03-31 | 国家能源投资集团有限责任公司 | Hydrogenation station control system and method and hydrogenation station |
| CN111350940A (en) * | 2020-03-13 | 2020-06-30 | 江苏安普特能源装备股份有限公司 | Hydrogenation control system and application method thereof |
| CN112413397A (en) * | 2020-11-18 | 2021-02-26 | 西安交通大学 | Pressurizing and filling device for hydrogenation station, and system and method using device |
| CN112413398A (en) * | 2020-11-19 | 2021-02-26 | 西安交通大学 | Hydrogenation system and method for hydrogenation station |
| CN112539340A (en) * | 2019-09-20 | 2021-03-23 | 中国石油化工股份有限公司 | Water electrolysis hydrogen supply hydrogenation station equipment model selection method |
| CN113090936A (en) * | 2021-03-19 | 2021-07-09 | 嘉寓氢能源科技(辽宁)有限公司 | Hydrogenation control method, system and device for uninterrupted power supply of hydrogen fuel cell |
| CN113090933A (en) * | 2020-01-08 | 2021-07-09 | 国家能源投资集团有限责任公司 | Control method of hydrogen filling station |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108613012A (en) * | 2016-12-09 | 2018-10-02 | 中国石油化工股份有限公司 | A kind of hydrogenation stations pneumatic type hydrogen compression gas storage system |
| CN109212247A (en) * | 2017-06-30 | 2019-01-15 | 深圳迈瑞生物医疗电子股份有限公司 | The feed liquid method of liquid feed device, sample analyser and liquid feed device |
| CN109210370A (en) * | 2018-09-18 | 2019-01-15 | 北京久安通氢能科技有限公司 | A kind of hydrogenation stations and hydrogenation control method |
| CN109237296A (en) * | 2018-09-21 | 2019-01-18 | 浙江昊凡科技有限公司 | A kind of hydrogen supply method and system applied to hydrogenation stations |
| CN110939860A (en) * | 2018-09-21 | 2020-03-31 | 国家能源投资集团有限责任公司 | Hydrogenation station control system and method and hydrogenation station |
| CN112539340B (en) * | 2019-09-20 | 2022-07-29 | 中国石油化工股份有限公司 | Water electrolysis hydrogen supply hydrogenation station equipment model selection method |
| CN112539340A (en) * | 2019-09-20 | 2021-03-23 | 中国石油化工股份有限公司 | Water electrolysis hydrogen supply hydrogenation station equipment model selection method |
| CN113090933A (en) * | 2020-01-08 | 2021-07-09 | 国家能源投资集团有限责任公司 | Control method of hydrogen filling station |
| CN111350940A (en) * | 2020-03-13 | 2020-06-30 | 江苏安普特能源装备股份有限公司 | Hydrogenation control system and application method thereof |
| CN112413397A (en) * | 2020-11-18 | 2021-02-26 | 西安交通大学 | Pressurizing and filling device for hydrogenation station, and system and method using device |
| CN112413397B (en) * | 2020-11-18 | 2021-11-23 | 西安交通大学 | Pressurizing and filling device for hydrogenation station, and system and method using device |
| CN112413398B (en) * | 2020-11-19 | 2021-11-23 | 西安交通大学 | Hydrogenation system and method for hydrogenation station |
| CN112413398A (en) * | 2020-11-19 | 2021-02-26 | 西安交通大学 | Hydrogenation system and method for hydrogenation station |
| CN113090936A (en) * | 2021-03-19 | 2021-07-09 | 嘉寓氢能源科技(辽宁)有限公司 | Hydrogenation control method, system and device for uninterrupted power supply of hydrogen fuel cell |
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