CN112050080B - Distributed control system, control method and measurement and control system for liquid hydrogen refueling station - Google Patents

Distributed control system, control method and measurement and control system for liquid hydrogen refueling station Download PDF

Info

Publication number
CN112050080B
CN112050080B CN202010961911.6A CN202010961911A CN112050080B CN 112050080 B CN112050080 B CN 112050080B CN 202010961911 A CN202010961911 A CN 202010961911A CN 112050080 B CN112050080 B CN 112050080B
Authority
CN
China
Prior art keywords
hydrogenation
pressure
liquid hydrogen
station
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.)
Active
Application number
CN202010961911.6A
Other languages
Chinese (zh)
Other versions
CN112050080A (en
Inventor
刘瑞敏
吴怀明
高婉丽
王孝
于海磊
王玉花
尚凯伦
李良
刘玉涛
杨思锋
王丽婧
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing Institute of Aerospace Testing Technology
Original Assignee
Beijing Institute of Aerospace Testing Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Beijing Institute of Aerospace Testing Technology filed Critical Beijing Institute of Aerospace Testing Technology
Priority to CN202010961911.6A priority Critical patent/CN112050080B/en
Publication of CN112050080A publication Critical patent/CN112050080A/en
Application granted granted Critical
Publication of CN112050080B publication Critical patent/CN112050080B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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
    • F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02—Discharging liquefied gases
    • F17C7/04—Discharging liquefied gases with change of state, e.g. vaporisation
    • 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
    • F17C13/002—Details of vessels or of the filling or discharging of vessels for vessels under 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
    • 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
    • F17C13/00—Details of vessels or of the filling or discharging of vessels
    • F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
    • F17C13/026—Special adaptations of indicating, measuring, or monitoring equipment having the temperature 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
    • F17C13/00—Details of vessels or of the filling or discharging of vessels
    • F17C13/12—Arrangements or mounting of devices for preventing or minimising the effect of explosion ; Other safety measures
    • F17C13/123—Arrangements or mounting of devices for preventing or minimising the effect of explosion ; Other safety measures for gas bottles, cylinders or reservoirs for tank vehicles or for railway tank wagons
    • 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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/05—Size
    • F17C2201/054—Size medium (>1 m3)
    • 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
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/01—Pure fluids
    • F17C2221/012—Hydrogen
    • 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
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146—Two-phase
    • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
    • 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
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/035—High pressure (>10 bar)
    • 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
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
    • F17C2225/0107—Single phase
    • F17C2225/0123—Single phase gaseous, e.g. CNG, GNC
    • 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
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/03—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
    • F17C2225/035—High pressure, i.e. between 10 and 80 bars
    • 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
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0135—Pumps
    • 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
    • F17C2250/036—Control means using alarms
    • 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
    • F17C2250/038—Control means using cameras
    • 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
    • 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
    • F17C2250/0631—Temperature
    • 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
    • F17C2260/00—Purposes of gas storage and gas handling
    • F17C2260/04—Reducing risks and environmental impact
    • F17C2260/042—Reducing risk of explosion
    • 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
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/06—Fluid distribution
    • F17C2265/063—Fluid distribution for supply of refuelling stations
    • 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
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0165—Applications for fluid transport or storage on the road
    • F17C2270/0181—Airbags
    • 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
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P90/00—Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
    • Y02P90/45—Hydrogen technologies in production processes

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

The invention discloses a distributed control system, a control method and a measurement and control system for a liquid hydrogen refueling station, wherein the control system comprises a master station system and a slave station system, the master station system comprises a station control system, and the slave station system comprises: the system comprises a liquid hydrogen storage device, a pump pressurization vaporization device, a high-pressure storage device, a hydrogenation unit, a safety monitoring device and a station control system, wherein the station control system is used for controlling a slave station system in a bus communication mode, monitoring and managing valves of a liquid hydrogen hydrogenation process system, storing data and inquiring data; the control method can simultaneously monitor each safety index of the liquid hydrogen hydrogenation process system in real time based on the control system, can give a fault alarm in time when any index is abnormal, and has high safety and reliability.

Description

Distributed control system, control method and measurement and control system for liquid hydrogen refueling station
Technical Field
The invention relates to the technical field of measurement and control, in particular to a distributed control system, a control method and a measurement and control system for a liquid hydrogen refueling station.
Background
The hydrogen station provides an infrastructure for energy supply for hydrogen energy utilization equipment facilities such as a hydrogen energy fuel cell and the like, and is a precondition for popularization and application of a hydrogen energy fuel cell automobile and acceleration of development of a hydrogen energy industry. Liquid hydrogen storage, namely a storage mode of increasing pressure by low-temperature liquid hydrogen, under a high-pressure state, the volume hydrogen storage density of the liquid hydrogen is increased along with the pressure rise, after the pressure of the liquid hydrogen at the temperature of 253 ℃ below zero is increased from 0.1MPa to 45MPa, the volume hydrogen storage density is increased from 70g/L to 100g/L, and the mass hydrogen storage density is thousands of times of the gas density. Compared with the liquid hydrogen storage under normal pressure, the hydrogen gas stored under high pressure and low temperature has small volatility and larger volume hydrogen storage density. Transferring the liquid hydrogen to a fixed liquid hydrogen container of the hydrogenation station by using a tank truck transportation mode to serve as a material supply source of the hydrogenation station; the gas hydrogen adopts a tube bundle vehicle as a hydrogen supply source, low-pressure liquid hydrogen in a storage tank is pressurized to 45MPa by a liquid hydrogen pump, the low-pressure liquid hydrogen enters a vaporizer for phase change heat exchange to form high-pressure hydrogen, the hydrogen of the tube bundle vehicle is pressurized to 45MPa by a liquid driving booster pump to form high-pressure hydrogen, and the high-pressure hydrogen is buffered and temporarily stored by a hydrogen storage cylinder and then is hydrogenated to a fuel cell vehicle. The monitoring control of the whole system of the liquid hydrogen hydrogenation station is lacked in the prior art, so that the state of the whole process system of the hydrogenation station cannot be timely and effectively controlled, and the whole health operation and maintenance are not facilitated.
Disclosure of Invention
Therefore, the technical problem to be solved by the invention is to overcome the defect that the monitoring control of the integral system of the liquid hydrogen refueling station is not lack and the integral healthy operation and maintenance is not facilitated in the prior art, so that a distributed control system, a control method and a measurement and control system of the liquid hydrogen refueling station are provided.
In order to achieve the purpose, the invention provides the following technical scheme:
in a first aspect, a distributed control system for a liquid hydrogen refueling station comprises: master station system and slave station system, master station system includes the station accuse system, and the slave station system includes: a liquid hydrogen storage device, a pump pressure-boosting vaporization device, a high-pressure storage device, a hydrogenation device and a safety monitoring device, wherein,
the station control system is used for controlling the slave station system in a bus communication mode, monitoring and managing a valve of the liquid hydrogen hydrogenation process system, and storing and inquiring data;
the liquid hydrogen storage device is used for storing liquid hydrogen and is used as a hydrogen supply source of the liquid hydrogen pump;
the pump pressurization vaporization device is used for carrying out pressurization vaporization on the high-pressure liquid hydrogen in the liquid hydrogen container;
the high-pressure storage device is used for storing high-pressure hydrogen and supplying the high-pressure hydrogen to the hydrogenation equipment;
the hydrogenation device is used for hydrogenating the hydrogen fuel automobile;
And the safety monitoring device is used for monitoring the state of the liquid hydrogen hydrogenation process system in real time and giving a fault alarm when an abnormality occurs.
In one embodiment, the liquid hydrogen storage device comprises a slave station controller, a liquid hydrogen container, a liquid level sensor and an electric valve, wherein the slave station controller is provided with a communication network interface and is communicated with the master station system through a preset communication protocol, so that the master station system can monitor the liquid hydrogen storage device in the whole process.
In one embodiment, a pump-pressurized vaporization apparatus, comprising: the controller is provided with a communication network interface and is communicated with a master station system through a preset communication protocol, so that the master station system carries out whole-process monitoring on the pump pressurization vaporization device.
In one embodiment, a high pressure storage device comprises: the system comprises a high-pressure hydrogen storage tank, a pressure sensor and an electric valve, wherein liquid hydrogen enters the hydrogen storage tank after being vaporized by a vaporizer, a master station PLC of a station control system of the high-pressure hydrogen storage system controls the electric valve of the high-pressure hydrogen storage tank, and the liquid hydrogen is distributed and supplied to a field hydrogenation system according to the hydrogen storage quantity obtained by the pressure sensor.
In one embodiment, the hydrotreater unit includes: the electronic controller sends out a control instruction to control the electric valve according to hydrogen supply pressure and temperature, hydrogen is supplied through the hydrogenation gun, the display screen displays corresponding flow, temperature and pressure parameters, the electronic controller is provided with a network interface system, and the electronic controller is communicated with the main control system through a preset protocol to enable the main station system to monitor the hydrogenation device.
In one embodiment, the electronic controller controls automatic leak detection in the hydrogenation process, automatically stores current data and continues to prolong display if power is suddenly cut off in the hydrogenation process, completes settlement when hydrogenation is performed, displays hydrogenation amount in real time according to actual hydrogenation needs, accumulates flow, automatically stops hydrogenation when the preset pressure is added, and performs safety interlocking and automatic shutdown when abnormal states occur in the hydrogenation process.
In one embodiment, the safety monitoring device comprises a video monitoring device and a hydrogen safety monitoring device, wherein:
the video monitoring device includes: the system comprises a hard disk video recorder, an explosion-proof camera and a communication power supply circuit, wherein the hard disk video recorder is used for monitoring whether a liquid hydrogen storage device leaks or not, whether a pump pressurization vaporization device operates normally or not, whether a high-pressure storage device is safe or not, and the working state of hydrogenation equipment and the state of a nearby environment in real time;
The hydrogen safety monitoring device comprises an explosion-proof hydrogen concentration probe and an explosion-proof flame detector which are both arranged above the process system, monitoring data is connected into the main control system, the main control system displays corresponding monitoring data, and a grading alarm of hydrogen concentration and an abnormal flame signal alarm are carried out.
In a second aspect, an embodiment of the present invention provides a distributed control method for a liquid hydrogen refueling station, where the distributed control system for a liquid hydrogen refueling station is based on the first aspect, and includes: the master station system controls the liquid hydrogen storage device, the pump pressurization vaporization device, the high-pressure storage device, the hydrogenation unit device and the safety monitoring device of the slave station system at the same time, wherein:
the control process for the liquid hydrogen storage device comprises the following steps: judging whether the main control system sends a signal for starting liquid hydrogen filling, if so, sequentially opening the manual control valve and the corresponding electromagnetic valve, monitoring whether the liquid level of the high-pressure hydrogen storage tank reaches a preset position, if so, sequentially closing the corresponding electromagnetic valve and the manual control valve, and if a signal for stopping liquid hydrogen filling is received in the process of liquid hydrogen filling, directly controlling to close the manual control valve;
the control process for the pump boosting vaporizing device comprises the following steps: after the running speed is preset, judging whether a main control system sends a signal for starting a cryogenic pump or not, if so, controlling the cryogenic pump to run stably, monitoring whether the state of the cryogenic pump is normal or not in the running process, if so, further monitoring whether the pressure at the outlet of a vaporizer is stable and normal or not, if so, opening a gas supply control valve, if receiving a signal for stopping the cryogenic pump sent by the main control system in the gas supply process, stopping supercharging, controlling to close the gas supply control valve, and if not, keeping the gas supply control valve in a closed state;
The control process for the high-voltage storage device comprises the following steps: judging whether the master control system sends a gas supply starting signal, if so, sequentially opening the manual control valve and the corresponding electromagnetic valve, monitoring whether the pressure of the high-pressure hydrogen storage tank reaches a preset threshold value, if so, sequentially closing the corresponding electromagnetic valve and the manual control valve, and if a gas supply stopping signal sent by the master control system is received in the gas supply process, directly controlling to close the manual control valve;
the control process for the hydrogenation unit comprises the following steps: judging whether the main control system sends a starting signal for starting a hydrogenation gun or not, if so, opening the gas source control valve, and if a starting signal for stopping the hydrogenation gun is received in the hydrogenation process, closing the gas source control valve and stopping gas supply;
the control process for the safety monitoring device comprises the following steps: simultaneously monitoring whether the hydrogen concentration and the liquid level and the pressure of the high-pressure hydrogen storage tank exceed preset thresholds; whether the temperature and the pressure of the cryopump are abnormal or not, and whether the pressure and the hydrogen concentration of the gas cylinder are normal or not; the hydrogenation pressure, the temperature and the hydrogen concentration are abnormal, and the state of the video monitoring equipment is abnormal; and sending out an alarm signal when at least one of the abnormal conditions is abnormal.
In a third aspect, an embodiment of the present invention provides a distributed measurement and control system for a liquid hydrogen refueling station, including: an information management system, a charging management system and a distributed control system of a liquid hydrogen refueling station according to the first aspect of the invention,
The information management system comprises a server and corresponding information management software, and performs process flow state display, key parameter curve display, alarm parameter display, video monitoring and equipment state monitoring by acquiring data acquired by the control system;
the charging management system measures, displays and settles the local gas filling amount through the data collected by the control system, and is also used for setting the gas filling amount and communicating with the hydrogenation device.
The technical scheme of the invention has the following advantages:
1. the invention provides a distributed control system and a control method for a liquid hydrogen refueling station, wherein the control system comprises a master station system and a slave station system, the master station system comprises a station control system, and the slave station system comprises: the system comprises a liquid hydrogen storage device, a pump pressurization vaporization device, a high-pressure storage device, a hydrogenation unit, a safety monitoring device and a station control system, wherein the station control system is used for controlling a slave station system in a bus communication mode, monitoring and managing valves of a liquid hydrogen hydrogenation process system, storing data and inquiring data; the control method can simultaneously monitor each safety index of the liquid hydrogen hydrogenation process system in real time based on the control system, can give a fault alarm in time when any index is abnormal, and has high safety and reliability.
2. The invention provides a distributed measurement and control system of a liquid hydrogen refueling station, which comprises: the embodiment of the invention provides an information management system, a charging management system and a distributed control system for a liquid hydrogen hydrogenation station, which can carry out control, management and metering charging on a hydrogenation process, and ensure the safe and stable operation of the whole system.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and other drawings can be obtained by those skilled in the art without creative efforts.
FIG. 1 is a block diagram of a distributed control system for a liquid hydrogen refueling station in an embodiment of the invention;
FIG. 2 is a communication connection diagram of a distributed control system of a liquid hydrogen refueling station provided in an embodiment of the invention;
FIG. 3 is a flow chart of a distributed control method for a liquid hydrogen refueling station provided in an embodiment of the present invention;
fig. 4 is a frame diagram of a distributed measurement and control system of a liquid hydrogen refueling station provided in an embodiment of the present invention.
Detailed Description
The technical solutions of the present invention will be described clearly and completely with reference to the accompanying drawings, and it is to be understood that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Furthermore, the technical features involved in the different embodiments of the present invention described below may be combined with each other as long as they do not conflict with each other.
Example 1
The embodiment of the invention provides a distributed control system for a liquid hydrogen refueling station, as shown in fig. 1, specifically comprising:
the system of master website and slave station, the system of master website includes the station accuse system, and the slave station system includes: a liquid hydrogen storage device, a pump pressure-boosting vaporization device, a high-pressure storage device, a hydrogenation device and a safety monitoring device, wherein,
and the station control system is used for controlling the slave station system in a bus communication mode, monitoring and managing valves of the liquid hydrogen hydrogenation process system, and storing and inquiring data. In the embodiment of the invention, the station control system comprises an engineer station, a master station PLC, network equipment and power supply equipment, wherein the master station PLC is installed in the engineer station, the network equipment and the power supply equipment are respectively used for communication and power supply of the master station PLC, the master station PLC monitors the pressure and temperature states of a hydrogen medium in real time, monitors the states of a valve and a pneumatic control valve, monitors the state parameters before and after the pump, records the times of switching the pump and the valve, and is used for fault diagnosis and equipment service life analysis, and when the parameters are monitored to be abnormal or faults occur, alarm information is sent.
In a specific embodiment, the station control system adopts domestic PLC-GCU521 equipment as a hardware platform, the equipment can include functions of CPU redundancy, communication network redundancy, power supply equipment redundancy and the like, and can have fault diagnosis and communication alarm functions, the GCU521 scanning period is 10ms, the equipment can be realized by communication devices COM521 and COM523, and communication protocols of Modbus RTU and Modbus TCP are supported, so that control over each device in the slave station system can be realized, monitoring and management of valves of each process system can be completed, and functions of data storage, data query and the like can be completed. The station control system is realized by adopting a domestic PLC-GCU521 controller, has the advantages of convenient programming, flexible use, high reliability, strong anti-interference capability and the like, is convenient to expand a hardware system in a device integration mode, can display each process flow chart and field process equipment state parameters in real time, can set alarm values and safety interlock control of each process system, can record current and previous alarm states, record curves, data reports and the like of each important parameter in real time, and is convenient to inquire data.
In the embodiment of the invention, a master station PLC of a station control system is provided with corresponding control management software, has a remote transmission interface, can realize remote data transmission and control through an optical fiber network, can adopt a domestic self-control software platform VxSCADA monitoring software and a configuration programming software, completes monitoring on a slave station system through the configuration programming, realizes the functions of realizing the data recording control flow, the safety chain and the like in the whole process from low-temperature liquid hydrogen at-253 ℃ to normal-temperature high-pressure gaseous hydrogen after pressurization and vaporization.
In the running process of monitoring software, the pressure and temperature states of a hydrogen medium are monitored in real time, the states of a valve and a pneumatic control valve are monitored, the state parameters before and after a pump are monitored, the times of opening and closing of the pump and the valve are recorded, the data parameters of the whole liquid hydrogen station system are subjected to data recording, data query and other functions through a data report function, the system can also be used for fault diagnosis and service life analysis, when the parameters are abnormal or faults occur, an audible and visual alarm is sent out, information is transmitted to the station control system, if the pressure value is abnormal, the pump or the valve is considered to be in fault, a fault processing program is started, and the corresponding control valve is opened and closed, so that the safety of a process system is ensured.
The liquid hydrogen storage device is used for storing liquid hydrogen and is used as a hydrogen supply source of the liquid hydrogen pump; in the embodiment of the invention, the liquid hydrogen storage device comprises a slave station controller, a liquid hydrogen container, a liquid level sensor and an electric valve, wherein the slave station controller is provided with a communication network interface and is communicated with a master station system through a preset communication protocol, so that the master station system can monitor the liquid hydrogen storage device in the whole process.
In a specific embodiment, the slave station controller adopts a domestic GCU321 controller, a communication network interface is provided, a ModbusTCP communication protocol is supported, and a field valve can be controlled, so that a liquid inlet function from a liquid hydrogen container to a liquid hydrogen pump inlet is completed. The GCU321 controller is communicated with the station control system through a Modbus TCP communication protocol, so that the whole-process monitoring function of the station control system on the liquid hydrogen storage system is realized.
The pump pressurization vaporization device is used for pressurizing and vaporizing the high-pressure liquid hydrogen in the liquid hydrogen container; in an embodiment of the present invention, a pump-pressurized vaporization apparatus includes: the controller is provided with a communication network interface and is communicated with a master station system through a preset communication protocol, so that the master station system carries out whole-process monitoring on the pump pressurization vaporization device.
In a specific embodiment, the SMART200 controller is used for controlling the frequency converter to realize the motor speed regulation control function and realize the corresponding action of the plunger pump, thereby completing the liquid pressurization function, and then exchanging heat through the vaporizer to change into high-pressure gas. The SMART200 controller is provided with a Profinet network interface and supports a Modbus TCP communication protocol, so that the whole-process monitoring function of the station control system on the pump pressurization system is realized.
The high-pressure storage device is used for storing high-pressure hydrogen and supplying the high-pressure hydrogen to the hydrogenation equipment; in an embodiment of the present invention, a high pressure hydrogen storage system comprises: the system comprises a high-pressure hydrogen storage tank, a pressure sensor and an electric valve, wherein liquid hydrogen enters the hydrogen storage tank after being vaporized by a vaporizer, a master station PLC-GCU521 of a station control system of the high-pressure hydrogen storage system controls the electric valve of the high-pressure hydrogen storage tank through a digital analog I/O interface, and the liquid hydrogen is distributed and supplied to an on-site hydrogenation system according to the hydrogen storage amount obtained by the pressure sensor.
The hydrogenation device is used for hydrogenating the hydrogen fuel automobile; in an embodiment of the invention, a hydrogenation apparatus comprises: the electronic controller sends out a control instruction to control the electric valve according to hydrogen supply pressure and temperature, hydrogen is supplied through the hydrogenation gun, the display screen displays corresponding flow, temperature and pressure parameters, the electronic controller is provided with a network interface system, and the electronic controller is communicated with the main control system through a preset protocol so that the main station system monitors the hydrogenation device.
In a specific embodiment, the electronic controller adopts an embedded STM32 singlechip and is provided with a network interface device, the network interface supports a modbus TCP communication protocol to realize communication with the station control system, and the station control system completes implementation monitoring. The electronic controller controls the automatic leakage detection of the hydrogenation process, if the power is suddenly cut off in the hydrogenation process, the current data is automatically stored and continuously displayed in an extended mode, the settlement of the hydrogenation is completed when the time is up, the hydrogenation amount is displayed in real time according to the actual hydrogenation requirement, the flow is accumulated, the hydrogenation is automatically stopped when the preset pressure is filled, and the safety interlocking and the automatic shutdown are carried out when the abnormal state occurs in the hydrogenation process.
The safety monitoring device is used for monitoring the state of the liquid hydrogen hydrogenation process system in real time and giving a fault alarm when an abnormality occurs; the embodiment of the invention comprises a video monitoring device and a hydrogen safety monitoring device;
the video monitoring device mainly comprises a hard disk video recorder, an explosion-proof camera and a communication power supply circuit, has video storage and playback functions, can be used for observing key positions of the liquid hydrogen storage device, the pump pressurization vaporization device, the high-pressure hydrogen storage device and the hydrogenation device, and is used for monitoring whether the liquid hydrogen storage device leaks, whether the pump pressurization vaporization device normally operates, whether the high-pressure storage device is safe, the working state of the hydrogenation device and the nearby environment state in real time, and the safe and stable operation on site is ensured.
The hydrogen safety monitoring device is mainly characterized in that a hydrogen concentration probe, a flame detector hydrogen concentration probe and a flame detector are arranged above a process system and all adopt explosion-proof products, the output signal of the hydrogen concentration probe is 0-100% of the corresponding range of a 4-20mA current signal, monitoring data acquired by the hydrogen safety monitoring device is connected into a main control system, the main control system displays corresponding monitoring data, and a hierarchical alarm of hydrogen concentration and an abnormal alarm of a flame signal are carried out. As shown in fig. 2, the master PLC and each slave PLC are communicatively connected by a corresponding connection interface.
The control system of the distributed control system of the liquid hydrogen refueling station provided by the embodiment of the invention comprises a master station system and a slave station system, wherein the master station system comprises a station control system, and the slave station system comprises: liquid hydrogen storage device, pump pressure boost vapourizing unit, high-pressure storage device, hydrogenation machine device and safety monitoring device, the station accuse system for control to the slave station system through bus communication mode carries out the control and the management of liquid hydrogen hydrogenation process system's valve, carry out data storage, data query, it is convenient that this control system can realize data sharing, flexible control, scalability is strong, can support a plurality of hydrogenation stations monitor control simultaneously, carry out fault alarm when appearing unusually, security and reliability are high.
Example 2
The embodiment of the invention provides a distributed control method for a liquid hydrogen refueling station, based on the control system in embodiment 1, a master station system simultaneously controls a liquid hydrogen storage device, a pump pressurization vaporization device, a high-pressure storage device, a hydrogenation unit and a safety monitoring device of a slave station system, and the whole control flow is shown in fig. 3, wherein:
the control process for the liquid hydrogen storage device comprises the following steps: judging whether the main control system sends a signal for starting liquid hydrogen filling, if so, sequentially opening the manual control valve and the corresponding electromagnetic valve, monitoring whether the liquid level of the high-pressure hydrogen storage tank reaches a preset position, if so, sequentially closing the corresponding electromagnetic valve and the manual control valve, and if a signal for stopping liquid hydrogen filling is received in the process of liquid hydrogen filling, directly controlling to close the manual control valve;
The control process for the pump pressurization vaporization device comprises the following steps: after the running speed is preset, judging whether a master control system sends a signal for starting a cryogenic pump or not, if so, controlling the cryogenic pump to run stably, monitoring whether the state of the cryogenic pump is normal or not in the running process, if so, further monitoring whether the pressure at the outlet of a vaporizer is stable and normal or not, if so, opening an air supply control valve, if receiving a signal for stopping the cryogenic pump sent by the master control system in the air supply process, stopping supercharging, controlling to close the air supply control valve, and if not, keeping the air supply control valve in a closed state;
the control process for the high-voltage storage device comprises the following steps: judging whether the master control system sends a gas supply starting signal, if so, sequentially opening the manual control valve and the corresponding electromagnetic valve, monitoring whether the pressure of the high-pressure hydrogen storage tank reaches a preset threshold value, if so, sequentially closing the corresponding electromagnetic valve and the manual control valve, and if a gas supply stopping signal sent by the master control system is received in the gas supply process, directly controlling to close the manual control valve;
the control process for the hydrogenation unit comprises the following steps: judging whether the main control system sends a starting signal for starting a hydrogenation gun or not, if so, opening the gas source control valve, and if a starting signal for stopping the hydrogenation gun is received in the hydrogenation process, closing the gas source control valve and stopping gas supply;
The control process for the safety monitoring device comprises the following steps: simultaneously monitoring whether the hydrogen concentration, the liquid level and the pressure of the high-pressure hydrogen storage tank exceed preset thresholds; whether the temperature and the pressure of the cryogenic pump are abnormal or not, and whether the pressure and the hydrogen concentration of the gas cylinder are normal or not; the hydrogenation pressure, the temperature and the hydrogen concentration are abnormal, and the state of the video monitoring equipment is abnormal; and sending out an alarm signal when at least one of the abnormal conditions is abnormal.
The distributed control method for the liquid hydrogen hydrogenation station, provided by the embodiment of the invention, is based on the control system, can simultaneously monitor each safety index of the liquid hydrogen hydrogenation process system in real time, can timely perform fault alarm when any index is abnormal, and has high safety and reliability.
Example 3
The embodiment of the invention provides a distributed measurement and control system for a liquid hydrogen refueling station, as shown in fig. 4, comprising: an information management system, a charging management system and a distributed control system of a liquid hydrogen refueling station according to the first aspect of the invention,
the information management system comprises a server and corresponding information management software, and performs process flow state display, key parameter curve display, alarm parameter display, video monitoring and equipment state monitoring by acquiring data acquired by the control system; a user can realize remote control and monitoring of the process flow and the process equipment through a WEB browser.
The charging management system measures, displays and settles the local gas filling amount through the data collected by the control system, and is also used for setting the gas filling amount and communicating with the hydrogenation device. The charging management system can support IC card charging, support receipt printing function, reserve an internet access interface to provide tax printing and the like.
The distributed measurement and control system provided by the embodiment of the invention can carry out control, management, metering and charging on the hydrogenation process, and ensures the safe and stable operation of the whole system.
It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. This need not be, nor should it be exhaustive of all embodiments. And obvious variations or modifications of the invention may be made without departing from the spirit or scope of the invention.

Claims (7)

1. A distributed control method of a liquid hydrogen hydrogenation station is based on a distributed control system of the liquid hydrogen hydrogenation station, and is characterized by comprising the following steps: the master station system controls the liquid hydrogen storage device, the pump pressurization vaporization device, the high-pressure storage device, the hydrogenation unit device and the safety monitoring device of the slave station system at the same time, wherein:
The control process for the liquid hydrogen storage device comprises the following steps: judging whether the main control system sends a signal for starting liquid hydrogen filling, if so, sequentially opening the manual control valve and the corresponding electromagnetic valve, monitoring whether the liquid level of the high-pressure hydrogen storage tank reaches a preset position, if so, sequentially closing the corresponding electromagnetic valve and the manual control valve, and if a signal for stopping liquid hydrogen filling is received in the process of liquid hydrogen filling, directly controlling to close the manual control valve;
the control process for the pump pressurization vaporization device comprises the following steps: after the running speed is preset, judging whether a main control system sends a signal for starting a cryogenic pump or not, if so, controlling the cryogenic pump to run stably, monitoring whether the state of the cryogenic pump is normal or not in the running process, if so, further monitoring whether the pressure at the outlet of a vaporizer is stable and normal or not, if so, opening a gas supply control valve, if receiving a signal for stopping the cryogenic pump sent by the main control system in the gas supply process, stopping supercharging, controlling to close the gas supply control valve, and if not, keeping the gas supply control valve in a closed state;
the control process for the high-voltage storage device comprises the following steps: judging whether the master control system sends a gas supply starting signal, if so, sequentially opening the manual control valve and the corresponding electromagnetic valve, monitoring whether the pressure of the high-pressure hydrogen storage tank reaches a preset threshold value, if so, sequentially closing the corresponding electromagnetic valve and the manual control valve, and if a gas supply stopping signal sent by the master control system is received in the gas supply process, directly controlling to close the manual control valve;
The control process for the hydrogenation unit comprises the following steps: judging whether the main control system sends a starting signal for starting a hydrogenation gun or not, if so, opening the gas source control valve, and if a starting signal for stopping the hydrogenation gun is received in the hydrogenation process, closing the gas source control valve and stopping gas supply;
the control process for the safety monitoring device comprises the following steps: simultaneously monitoring whether the hydrogen concentration and the liquid level and the pressure of the high-pressure hydrogen storage tank exceed preset thresholds; whether the temperature and the pressure of the cryogenic pump are abnormal or not, and whether the pressure and the hydrogen concentration of the gas cylinder are normal or not; the hydrogenation pressure, the temperature and the hydrogen concentration are abnormal, and the state of the video monitoring equipment is abnormal; when at least one of the abnormal conditions is abnormal, an alarm signal is sent out;
liquid hydrogen hydrogenation station distributed control system includes: the system of master website and slave station, the system of master website includes the station accuse system, and the slave station system includes: a liquid hydrogen storage device, a pump pressure-boosting vaporization device, a high-pressure storage device, a hydrogenation device and a safety monitoring device, wherein,
the station control system is used for controlling the slave station system in a bus communication mode, monitoring and managing a valve of the liquid hydrogen hydrogenation process system, and storing and inquiring data;
the liquid hydrogen storage device is used for storing liquid hydrogen and is used as a hydrogen supply source of the liquid hydrogen pump;
The pump pressurization vaporization device is used for carrying out pressurization vaporization on the high-pressure liquid hydrogen in the liquid hydrogen container;
the high-pressure storage device is used for storing high-pressure hydrogen and supplying the high-pressure hydrogen to the hydrogenation equipment;
the hydrogenation device is used for hydrogenating the hydrogen fuel automobile;
the safety monitoring device is used for monitoring the state of the liquid hydrogen hydrogenation process system in real time and giving a fault alarm when an abnormality occurs;
the station control system comprises: engineer station, main website PLC, network equipment, power supply unit, install main website PLC in engineer station, network equipment and power supply unit are used for main website PLC respectively to communicate and the power supply, main website PLC real time monitoring hydrogen medium pressure, the temperature state, monitoring valve, gas accuse valve state, before the monitoring pump, behind the pump state parameter, record pump, the valve number of times of opening and shutting, be used for failure diagnosis and equipment life analysis, when the parameter is unusual or breaks down in the control, send alarm information.
2. The distributed control method of the liquid hydrogen refueling station as claimed in claim 1, wherein the liquid hydrogen storage device comprises a slave station controller, a liquid hydrogen container, a liquid level sensor and an electric valve, and the slave station controller is provided with a communication network interface and communicates with the master station system through a preset communication protocol, so that the master station system can monitor the liquid hydrogen storage device in the whole process.
3. The distributed control method for the liquid hydrogen refueling station as recited in claim 1, wherein the pump pressurization vaporizing device comprises: the controller is provided with a communication network interface and is communicated with a master station system through a preset communication protocol, so that the master station system can monitor the pump pressurization vaporization device in the whole process.
4. The distributed control method of the liquid hydrogen refueling station as recited in claim 1, wherein the high pressure storage device includes: the system comprises a high-pressure hydrogen storage tank, a pressure sensor and an electric valve, wherein liquid hydrogen enters the hydrogen storage tank after being vaporized by a vaporizer, a master station PLC of the station control system of the high-pressure hydrogen storage system controls the electric valve of the high-pressure hydrogen storage tank, and the liquid hydrogen is distributed and supplied to the field hydrogenation system according to the hydrogen storage quantity obtained by the pressure sensor.
5. The distributed control method of a liquid hydrogen refueling station as recited in claim 1, wherein the hydrotreater device includes: the electronic controller sends out a control instruction to control the electric valve according to hydrogen supply pressure and temperature, hydrogen is supplied through the hydrogenation gun, the display screen displays corresponding flow, temperature and pressure parameters, the electronic controller is provided with a network interface system, and the electronic controller is communicated with the main control system through a preset protocol so that the main station system monitors the hydrogenation device.
6. The distributed control method of the liquid hydrogen refueling station as claimed in claim 5, wherein the electronic controller controls automatic leak detection in the hydrogenation process, automatically stores current data and continues to prolong display if power is suddenly cut off in the hydrogenation process, completes secondary hydrogenation settlement, displays the hydrogenation amount in real time according to the actual hydrogenation requirement, accumulates the flow, automatically stops hydrogenation when the preset pressure is reached, and is safely interlocked and automatically stopped when abnormal conditions occur in the hydrogenation process.
7. The distributed control method of the liquid hydrogen refueling station as recited in claim 1, wherein the safety monitoring device comprises a video monitoring device and a hydrogen safety monitoring device, wherein:
the video monitoring device includes: the system comprises a hard disk video recorder, an explosion-proof camera and a communication power supply circuit, wherein the hard disk video recorder is used for monitoring whether a liquid hydrogen storage device leaks or not, whether a pump pressurization vaporization device operates normally or not, whether a high-pressure storage device is safe or not, and the working state of hydrogenation equipment and the state of a nearby environment in real time;
the hydrogen safety monitoring device comprises an explosion-proof hydrogen concentration probe and an explosion-proof flame detector which are both arranged above the process system, monitoring data is connected into the main control system, the main control system displays corresponding monitoring data, and a grading alarm of hydrogen concentration and an abnormal flame signal alarm are carried out.
CN202010961911.6A 2020-09-14 2020-09-14 Distributed control system, control method and measurement and control system for liquid hydrogen refueling station Active CN112050080B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010961911.6A CN112050080B (en) 2020-09-14 2020-09-14 Distributed control system, control method and measurement and control system for liquid hydrogen refueling station

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010961911.6A CN112050080B (en) 2020-09-14 2020-09-14 Distributed control system, control method and measurement and control system for liquid hydrogen refueling station

Publications (2)

Publication Number Publication Date
CN112050080A CN112050080A (en) 2020-12-08
CN112050080B true CN112050080B (en) 2022-05-24

Family

ID=73611690

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010961911.6A Active CN112050080B (en) 2020-09-14 2020-09-14 Distributed control system, control method and measurement and control system for liquid hydrogen refueling station

Country Status (1)

Country Link
CN (1) CN112050080B (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113339699A (en) * 2021-05-10 2021-09-03 上海氢枫能源技术有限公司 Digital diagnosis system and method for hydrogenation station
CN113926370A (en) * 2021-07-29 2022-01-14 四川宏华电气有限责任公司 Distributed liquid supply sand mixing sledge
CN113790389B (en) * 2021-09-08 2022-11-04 上海氢枫能源技术有限公司 Method and system for adjusting chilled water flow of water chilling unit of hydrogen station
CN115343086B (en) * 2022-08-04 2024-05-03 上海智能新能源汽车科创功能平台有限公司 Online pre-detection method and system for high-pressure hydrogenation machine
CN116256470B (en) * 2023-01-16 2023-11-28 南京市燃气工程设计院有限公司 Hydrogen quality on-line analysis system based on hydrogen adding station
CN118167917A (en) * 2023-06-29 2024-06-11 国网上海市电力公司 Hydrogen production and hydrogenation system of hydrogenation station and control method thereof
CN118331165A (en) * 2024-04-26 2024-07-12 中太能源科技(上海)有限公司 Remote monitoring and control system of hydrogen liquefaction factory

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5759741B2 (en) * 2011-02-16 2015-08-05 岩谷産業株式会社 Hydrogen gas filling device for fuel and hydrogen gas filling method for fuel
CN206563175U (en) * 2017-02-27 2017-10-17 广州协鑫蓝天燃气热电有限公司 A kind of GTCC power plant LNG Vaporizing Station control system
CN207196076U (en) * 2017-09-12 2018-04-06 张家港富瑞氢能装备有限公司 A kind of hydrogen-feeding system at liquid hydrogen high-pressure hydrogenation station
CN107968213A (en) * 2017-11-29 2018-04-27 同济大学 Hydrogen supply control device
CN110413030B (en) * 2019-08-02 2021-04-13 上海舜华新能源系统有限公司 Management system of hydrogenation station master control cabinet
CN110953480B (en) * 2019-12-12 2021-06-29 重庆耐德能源装备集成有限公司 Safe and rapid hydrogenation machine, hydrogenation system, hydrogenation station and hydrogenation method
CN111457246B (en) * 2020-04-01 2021-12-17 江苏国富氢能技术装备股份有限公司 Hydrogen storage type hydrogen filling station

Also Published As

Publication number Publication date
CN112050080A (en) 2020-12-08

Similar Documents

Publication Publication Date Title
CN112050080B (en) Distributed control system, control method and measurement and control system for liquid hydrogen refueling station
CN110375196B (en) Management system of hydrogenation station service cabinet
CN109491341B (en) Monitoring and data analysis system for oil field operation equipment
CN104006289A (en) Skid-mounting full integration LNG and LCNG remote monitor unattended filling station
CN203488979U (en) Skid-mounted full-integrated LNG (Liquefied Natural Gas) and LCNG (Liquefied Compressed Natural Gas) remote control monitored unattended filling station
CN114123490A (en) Offshore wind power comprehensive energy monitoring system and method
CN110413030A (en) A kind of management system of hydrogenation stations control cabinet
CN111681396A (en) Vehicle-mounted liquid hydrogen bottle ground test system and test method
CN105443982A (en) Intelligent LNG gasifying skid with remote monitoring function
CN115123588A (en) Rocket ground filling control system and control method
CN112526043A (en) Transformer oil chromatography on-line monitoring carrier gas warning device and application method
CN106774073A (en) A kind of SF6 electrical equipments automatic air supply device long distance control system
CN112253999B (en) Hydrogen storage device management system, intelligent replacement method and device
CN218957072U (en) Control system of hydrogen adding station
CN104019373A (en) Skid-mounted fully-integrated LNG and LCNG on-site sub-station ESD system
CN114963013B (en) Management method and system for monitoring urban gas operation state based on Internet of things platform
CN213954989U (en) L-CNG remote diagnosis system
CN114166410A (en) Transformer substation oil chromatogram carrier gas pressure monitoring alarm and uninterrupted switching device
CN113864635A (en) Small storage tank gas supply method and system
CN115562094A (en) Liquid hydrogen preparation system based on digital twinning
CN118362439B (en) Remote monitoring device, system and method for durability test of liquefied gas storage tank
CN220874270U (en) Intelligent power supply system for crude oil pipeline
CN112097099A (en) System architecture of intelligent medical air supply device and control method thereof
CN117553998B (en) Static pressure constant voltage device and method for transformer
CN219912661U (en) Data communication terminal with local monitoring and remote transmission functions and air supply system thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant