CN110985881A - Gas filling system and filling method - Google Patents

Gas filling system and filling method Download PDF

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Publication number
CN110985881A
CN110985881A CN201911294012.9A CN201911294012A CN110985881A CN 110985881 A CN110985881 A CN 110985881A CN 201911294012 A CN201911294012 A CN 201911294012A CN 110985881 A CN110985881 A CN 110985881A
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CN
China
Prior art keywords
pipeline
gas
valve
compressor
filling
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Pending
Application number
CN201911294012.9A
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Chinese (zh)
Inventor
雷琦
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Shanghai Pujiang Specialty Gases Co ltd
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Shanghai Pujiang Specialty Gases Co ltd
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Priority to CN201911294012.9A priority Critical patent/CN110985881A/en
Publication of CN110985881A publication Critical patent/CN110985881A/en
Pending legal-status Critical Current

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    • 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
    • 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
    • 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
    • F17C13/04—Arrangement or mounting of valves
    • 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
    • F17C2223/0107—Single phase
    • F17C2223/0123—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
    • 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
    • F17C2223/036—Very high pressure (>80 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
    • 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
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0165—Applications for fluid transport or storage on the road
    • F17C2270/0168—Applications for fluid transport or storage on the road by vehicles
    • F17C2270/0178—Cars
    • 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

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  • 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 gas filling system, which comprises a gas source, a pipeline system and a control system, wherein the gas source is connected with the pipeline system; the pipeline system comprises a gas filling pipeline system, the gas filling pipeline system comprises a first pipeline directly connected with a gas source and a vehicle to be filled, the gas filling pipeline system further comprises a compressor connected to the first pipeline, a second pipeline is connected between the inlet end and the outlet end of the compressor, and the second pipeline comprises a second pneumatic valve. According to the gas filling system and the gas filling method, when gas is filled initially, gas filling is directly carried out on a vehicle to be filled through the first pipeline, when the pressure of the vehicle to be filled is balanced with that of a gas source, the vehicle is filled through gas suction of the compressor, the gas filling time of the vehicle is greatly shortened by combining two gas filling modes of direct gas filling of the first pipeline of the gas source and gas suction of the compressor, and after gas filling is completed, the compressor is subjected to internal circulation, so that damage to a machine caused by the fact that the compressor is normally opened and normally closed is avoided.

Description

Gas filling system and filling method
Technical Field
The invention relates to a gas filling technology, which is particularly suitable for filling hydrogen.
Background
Hydrogen energy is receiving unprecedented attention as a clean energy source. The combustion heat value is high, the energy density of hydrogen energy occupies absolute advantage from the viewpoint of energy density, the hydrogen is used as a raw material, the basic energy density is 3 times that of gasoline, the work-doing efficiency of a motor is 2 times that of an internal combustion engine, the actual density is 6 times that of gasoline, and the advantage is obvious. And from the history of energy evolution of human in the past hundred years, the history is essentially the adjustment history of the carbon-hydrogen ratio, and the higher the hydrogen content is, the higher the energy density is. In addition, the combustion product of hydrogen energy is water, so that the environment is not polluted.
The main principle of the hydrogen energy fuel cell vehicle is that hydrogen gas generates electrochemical reaction in the fuel cell to generate electric energy to drive the vehicle to run, so that an internal combustion engine is not used, and the energy efficiency is higher. The fuel cell here is not an energy storage cell in the general sense of us, but a place where energy conversion takes place. In the popularization and application of pure electric vehicles, the most people who spit the grooves are short in endurance mileage and long in charging time. These problems do not exist for hydrogen fuel cell vehicles: according to the practical application at home and abroad, the constant-speed endurance mileage of a household fuel cell automobile with a 120L hydrogen energy gas storage tank can exceed 600 kilometers, and the actual working condition endurance mileage can also break through 450 kilometers.
In the aspect of fuel supplement, the domestic conventional hydrogenation is carried out, the process operation flow is that the suction air source of a compressor adopts a long tube trailer with the highest pressure of 20MPA and the actual pressure of 18-19MPa as the air source, in this way, when the air source pressure is highest, one vehicle is filled by two gas storage bottle hydrogen energy vehicles according to the pressurization of 30MPa and 7.5Kg, when the air source pressure is at a high position, about 6 minutes are needed for filling 1 vehicle, and when the pressure of the long tube trailer of the air source is reduced to a low position, at least 15 minutes are needed for filling 1 vehicle. The hydrogen filling technology has unstable inflation time due to unstable air source pressure, so a set of quick, safe and reliable hydrogen energy filling technology is needed to realize the purpose of supplementing hydrogen fuel to a fuel cell automobile like refueling.
Disclosure of Invention
The invention provides a gas filling system which can solve the defects in the prior art.
The technical scheme of the invention is as follows:
a gas filling system comprises a gas source, a pipeline system and a control system; wherein the content of the first and second substances,
the pipeline system comprises an air charging pipeline system, a replacement pipeline system and an emptying pipeline system; the air filling pipeline system comprises a first pipeline for connecting the air source with a vehicle to be filled, the first pipeline is provided with a first pressure gauge and a first pneumatic valve, the first pressure gauge is used for detecting air pressure, the inlet end of the first pressure gauge is connected with the outlet of the air source, and the outlet end of the first pressure gauge is connected with the inlet end of the first pneumatic valve; the rear end of the first pneumatic valve is also provided with a third pneumatic valve and a second pressure gauge, the outlet end of the first pneumatic valve is connected with the inlet end of the third pneumatic valve, the outlet end of the third pneumatic valve is connected with the second pressure gauge, and the outlet end of the second pressure gauge is connected with at least one air gun;
the outlet end of the first pneumatic valve is also connected with a compressor, and the outlet end of the compressor is connected with the inlet end of the third pneumatic valve; the gas adding pipeline system also comprises a second pipeline, the second pipeline is connected with the inlet end of the compressor and the outlet end of the compressor, and the second pipeline is provided with a second pneumatic valve;
the control system comprises a safety monitoring system and an electrical control system; the electric control system comprises a controller and a man-machine exchange interface, the controller is respectively electrically connected with the first pneumatic valve, the second pressure gauge and the third pneumatic valve, when the pressure value of the second pressure gauge exceeds 35MPa, an electric signal is sent to the controller, the controller controls the third pneumatic valve to be closed and the second pneumatic valve to be opened according to the received signal, gas filling is finished at the moment, and gas circulates between the compressor and the second pipeline. When the pressure value detected by the second pressure gauge is less than 30MPa, an electric signal is sent to the controller, the controller controls the second pneumatic valve to be closed and the third pneumatic valve to be opened according to the size of the received signal, and the compressor enters a gas filling state.
When the pressure of the gas source is higher, the vehicle to be filled is directly filled with gas through the first pipeline, and the gas is filled by utilizing the pressure difference between the gas source and the vehicle to be filled, so that the initial filling speed is improved; when the pressure of a vehicle gas cylinder to be filled is balanced with the pressure of a gas source, gas is filled by sucking gas through a compressor; the gas source directly adds gas through the first pipeline and combines the compressor to add gas, thereby greatly improving the filling amount of the gas filling system, shortening the gas adding time and improving the gas adding efficiency. And meanwhile, when gas filling is finished, the compressor is not required to be shut down, the third pneumatic valve is shut down, the second pneumatic valve is started, gas is circulated between the compressor and the second pipeline, damage to a machine caused by normal opening and closing of the compressor is avoided, and after the compressor is shut down, inert gas replacement is required to be carried out on the system again when the compressor is restarted.
The first pressure gauge is a pressure transmitter with the model number of EJA530E-JBS4N-017DL/NF 2Z; the second pressure gauge is a pressure transmitter with model number of EJX630A-EDS4N-017DL/NF 2/A1/Z. The first pressure gauge and the second pressure gauge are respectively and electrically connected with the controller, convert the gas pressure signal into an electric signal and feed back to the controller.
Preferably, the replacement pipeline system comprises an inert gas source, such as nitrogen, stored in a nitrogen cylinder, and a replacement pipeline connecting the inert gas source and the pipeline system; the replacement pipeline comprises a first replacement pipeline and a second replacement pipeline, wherein the first replacement pipeline is connected with the outlet end of the inert gas source and the inlet end of the first pressure gauge, and the second replacement pipeline is connected with the outlet end of the inert gas source and the inlet end of the third pneumatic valve; the first replacement pipeline is provided with a first stop valve, and the second replacement pipeline is provided with a second stop valve; the first stop valve is used for controlling the on-off of the first replacement pipeline, and the second stop valve is used for controlling the on-off of the second replacement pipeline.
The emptying pipeline system comprises: a first vent pipe connected with the outlet end of the first pressure gauge, a second vent pipe connected with the outlet end of the compressor, and a third vent pipe connected with the outlet end of the second pressure gauge; the first emptying pipe is provided with a first emptying valve, the second emptying pipe is provided with a second emptying valve, and the third emptying pipe is provided with a third emptying valve. The first emptying pipe, the second emptying pipe and the third emptying pipe are used for emptying gas in the pipeline when the gas filling pipeline system performs inert gas replacement and hydrogen gas replacement, and emptying gas in the gas filling pipeline system when the compressor stops. The first emptying valve, the second emptying valve and the third emptying valve are used for controlling the on-off of corresponding pipelines.
Preferably, the safety monitoring system includes: the gas probe and the flame probe are respectively and electrically connected with a controller of the control system. The gas probe is used for detecting the gas concentration and feeding back the information of the detected gas concentration to the controller, specifically, the gas probe sends an electric signal to the controller, and the controller judges whether gas leakage is detected according to the size of the electric signal and controls to send out an alarm prompt. And similarly, the flame probe sends an electric signal to the controller, and the controller judges whether to send out a flame alarm prompt according to the size of the electric signal.
Preferably, the control system comprises an alarm electrically connected with the controller.
Preferably, the gas source is a hydrogen long-tube trailer, and the gas source pressure of the hydrogen long-tube trailer is 15-20 MPa; and the outlet end of the second pressure gauge is also connected with a flowmeter for detecting the gas flow.
Preferably, a bypass valve is further arranged on the first pipeline, is arranged between the first pneumatic valve and the third pneumatic valve and is used for controlling the on-off of the first pipeline when an air source directly hydrogenates a vehicle to be filled through the first pipeline.
A gas filling method using the gas filling system according to any one of the above, comprising the steps of:
(1) replacing the air adding pipeline system with inert gas for 3-5 times, wherein the inert gas is replaced by air in the air adding pipeline system;
(2) replacing the gas to be inflated in the gas filling pipeline system, replacing nitrogen in the gas filling pipeline system with the gas to be inflated, and performing gas leakage detection on the gas filling pipeline system for 3-5 times;
(3) safety inspection before gas filling is carried out, open fire and fire operation around the gas filling are ensured, and electrostatic grounding is carried out;
(4) and filling gas into the vehicle to be filled, closing the third pneumatic valve and opening the second pneumatic valve after filling gas, and circulating the gas between the compressor and the second pipeline.
After the air is added, the controller controls the third pneumatic valve to be automatically closed and the second pneumatic valve to be automatically opened, so that the air circulates between the compressor and the second pipeline, the compressor enters an internal circulation mode, the compressor does not need to be repeatedly opened and closed, the damage to the compressor caused by the normal opening and the normal stopping of the compressor is avoided, and the compressor is protected; meanwhile, when the compressor enters an internal circulation mode, the variable-frequency low-energy-consumption operation is carried out, and the energy consumption of the system operation is reduced.
Preferably, during hydrogenation, when the pressure of a gas cylinder of a vehicle to be filled is smaller than the pressure of a gas source, the vehicle to be filled is filled with gas by adopting the first pipeline, the initial gas filling speed is increased, when the pressure of the gas cylinder of the vehicle to be filled is balanced with the pressure of the gas source, the compressor is started, and the gas is filled into the vehicle to be filled by adopting the compressor.
Preferably, during hydrogenation, the second pneumatic valve is ensured to be closed, and meanwhile, the first pipeline is adopted and the compressor is started to charge the vehicle to be charged.
Preferably, the alarm threshold of the first pressure gauge is set to be 25MPa, the alarm threshold of the second pressure gauge is set to be 37MPa, and the alarm threshold of the hydrogen probe is set to be 10%. When the actual pressure value detected by the first pressure gauge exceeds 25MPa, or the actual pressure value detected by the second pressure gauge exceeds 37MPa, or the actual value of the hydrogen probe exceeds 10% and is less than 25%, the controller controls the alarm to give an alarm. And when the actual value of the hydrogen probe exceeds 25%, the controller controls the alarm to send an alarm, and shuts down the human-machine exchange interface, the compressor, the first pneumatic valve, the second pneumatic valve and the third pneumatic valve.
Preferably, the controller comprises a knob switch electrically connected with the controller. The knob switch is used for controlling the compressor to enter a frequency conversion internal circulation state and waking up the compressor to enter a hydrogenation state, and the compressor normally works in the hydrogenation state. The knob switch comprises a bypass position and a hydrogenation position, when the knob switch is turned to the hydrogenation position, the compressor enters a hydrogenation state, the knob switch is turned to the bypass position, and at the moment, the compressor enters an inner circulation state.
Preferably, step (1) comprises: and opening the first replacement pipeline to fill inert gas into the first section of pipeline, wherein the first section of pipeline refers to a pipeline between the outlet end of the gas source outlet main valve and the inlet end of the first emptying pipe, when the first pressure gauge indicates that the pipeline pressure reaches 0.5MPa, the inert gas filling is stopped, the first emptying valve is opened, the pressure is relieved through the first emptying pipeline, and the first section of pipeline is repeatedly replaced for 3-8 times according to the method.
And opening the first replacement pipeline to fill inert gas into the second pipeline, wherein the second pipeline refers to a pipeline between the first pneumatic valve and the third pneumatic valve on the first pipeline, stopping filling the inert gas when the pressure of the pipeline is indicated to reach 0.5MPa by the first pressure gauge PIT-101, opening the second vent valve, and releasing pressure through the second vent pipeline, and according to the method, repeatedly replacing the second pipeline for 3-8 times. And opening the third replacement pipeline to fill inert gas into a third section of pipeline, wherein the third section of pipeline refers to a pipeline between the rear end of the third pneumatic valve and the air gun, when the pressure of the pipeline indicated by the second pressure gauge reaches 0.5MPa, the inert gas filling is stopped, a third emptying valve is opened, the pressure is relieved through the third emptying pipeline, and according to the method, the third section of pipeline is repeatedly replaced for 3-8 times to finish the inert gas replacement of the air filling pipeline system.
The inert gas can be nitrogen, and the air in the gas filling pipeline system is replaced by the inert gas, so that the purity of the gas filled in the vehicle to be filled is ensured, and the safety of the gas filling system and the vehicle to be filled is ensured.
The gas filling system is suitable for hydrogen filling, is particularly suitable for hydrogen filling of hydrogen energy vehicles for internal commuting, is also suitable for filling of other gases such as natural gas, and is not limited in the above.
Compared with the prior art, the invention has the following beneficial effects:
firstly, the gas filling system and the filling method comprise an air source long-tube trailer, the pressure of the air source long-tube trailer is ensured to be between 15 and 20MPa, and the suction pressure of a compressor is greatly improved, namely the suction capacity is improved; meanwhile, when the pressure of the vehicle-mounted gas cylinder of the vehicle to be filled is lower than 15MPa, the gas source long-tube trailer is adopted to directly fill the gas through the first pipeline, so that the initial filling speed is greatly improved; when the pressure of a vehicle-mounted gas cylinder of the vehicle to be filled is balanced with the pressure of the gas source long pipe trailer, starting a compressor, and sucking a gas source by the compressor to fill the vehicle to be filled; when the subsequent vehicle is filled, the first pipeline of the air source long pipe trailer is directly filled and a filling method of sucking the air source by combining a compressor is adopted, so that the filling time is shortened, and the filling efficiency is improved.
Secondly, the inlet end and the outlet end of the compressor are communicated through a second pipeline, when the pressure of a second pressure gauge is increased to 35MPa, the controller controls a third pneumatic valve to be automatically closed and opens a second pneumatic valve, so that gas circulates between the compressor and the second pipeline, the compressor enters an internal circulation mode, the compressor does not need to be repeatedly opened and closed, and the damage to the compressor caused by normal opening and normal stopping of the compressor is avoided; meanwhile, when the compressor enters an internal circulation mode, the variable-frequency low-energy-consumption operation is carried out, so that the compressor is protected; in addition, when the subsequent vehicle needs to be aerated, the hydrogenation can be started only by turning the knob switch to the hydrogenation position, the process is simple, the operation is convenient, the aeration process of the aeration station is more stable, and the commercialization of the aeration station is easier.
Of course, it is not necessary for any product in which the invention is practiced to achieve all of the above-described advantages at the same time.
Drawings
FIG. 1 is a schematic view of a gas-filling piping system according to embodiment 1 of the present invention;
FIG. 2 is another schematic view of the gas supply piping system according to embodiment 1 of the present invention;
FIG. 3 is a schematic view of a gas filling system of embodiment 1 of the invention;
FIG. 4 is a schematic diagram of a hydrogenation scheme in example 2 of the present invention.
Detailed Description
The invention will be further illustrated with reference to the following specific examples. It should be understood that these examples are only for illustrating the present invention and are not intended to limit the scope of the present invention. In practice, the invention will be understood to cover all modifications and variations of this invention provided they come within the scope of the appended claims.
Example 1
The embodiment provides a gas filling system, which comprises a gas source 1, a pipeline system and a control system, and is shown in fig. 1; wherein the content of the first and second substances,
the pipeline system comprises an air charging pipeline system, a replacement pipeline system and an emptying pipeline system; the gas filling pipeline system comprises a first pipeline 11 for connecting a gas source 1 and a vehicle to be filled, the first pipeline 11 is provided with a first pressure gauge PIT-101 and a first pneumatic valve PBV-101 for detecting gas pressure, the inlet end of the first pressure gauge PIT-101 is connected with the outlet of the gas source, and the outlet end of the first pressure gauge PIT-101 is connected with the inlet end of the first pneumatic valve PBV-101; the rear end of the first pneumatic valve PBV-101 is also provided with a third pneumatic valve PBV-103 and a second pressure gauge PIT-102, the outlet end of the first pneumatic valve PBV-101 is connected with the inlet end of the third pneumatic valve PBV-103, the outlet end of the third pneumatic valve PBV-103 is connected with the second pressure gauge PIT-102, and the outlet end of the second pressure gauge PBV-102 is connected with at least one air gun 2;
the outlet end of the first pneumatic valve PBV-101 is also connected with a compressor 40, and the outlet end of the compressor 40 is connected with the inlet end of a third pneumatic valve PBV-103; the air-adding pipeline system also comprises a second pipeline 12, the second pipeline 12 is respectively communicated with the inlet end and the outlet end of the compressor 40, the two ends of the second pipeline are also respectively communicated with the first pipeline 11, and a second air-operated valve PBV-102 is arranged on the second pipeline 12;
the control system comprises a safety monitoring system and an electrical control system; the electric control system comprises a controller and a man-machine exchange interface, the controller is respectively electrically connected with the first pressure gauge PIT-101, the first pneumatic valve PBV-101, the second pneumatic valve PBV-102, the second pressure gauge PIT-102 and the third pneumatic valve PBV-103, and the controller receives an electric signal sent by the second pressure gauge PIT-102 and controls the opening and closing of the first pneumatic valve PBV-101, the second pneumatic valve PBV-102 and the third pneumatic valve PBV-103 according to the size of the electric signal. Specifically, first manometer PIT-101 is used for showing the pressure value of hydrogen long-tube trailer export to convert the pressure value into the signal of telecommunication, feed back to the controller, the controller judges whether the pressure value of hydrogen long-tube trailer export is in safety range according to the size of the signal of telecommunication received, ensures the security of system. The second pressure gauge PIT-102 is used for detecting the pressure value of the front end of the vehicle to be filled, when the pressure detected by the second pressure gauge PIT-102 is larger than 35MPa, the vehicle to be filled is full, the PIT-102 sends an electric signal to the controller, the controller controls the third pneumatic valve PBV-103 to be closed according to the size of the received electric signal, the vehicle to be filled is stopped from being inflated, meanwhile, the PBV-102 is opened, the compressor does not need to be closed, hydrogen circulates between the compressor and the second pipeline 12, and damage to the compressor caused by the fact that the compressor is normally open and normally closed is avoided. When the pressure detected by the second pressure gauge PIT-102 is less than 30MPa, the pressure of hydrogen in the vehicle to be filled is insufficient, the PIT-102 sends an electric signal to the controller, the controller controls the second pneumatic valve PBV-102 to be closed and the third pneumatic valve PBV-103 to be opened according to the received electric signal, circulation of hydrogen between the compressor and the second pipeline 12 is cut off, and the vehicle to be filled can be inflated at the moment. The hydrogen circulates between the compressor and the second pipeline, so that when a subsequent vehicle needs hydrogenation, inert gas replacement is not needed to be carried out on the gas adding pipeline system again, and direct hydrogenation can be carried out.
Meanwhile, when the pressure of the second pressure gauge is increased to 35MPa, the hydrogenation is finished, the controller controls the third pneumatic valve PBV-103 to be automatically closed and opens the second pneumatic valve PBV-102, so that gas circulates between the compressor and the second pipeline 12, the compressor enters an internal circulation mode, the compressor does not need to be repeatedly opened and closed, the damage to the compressor caused by normal opening and normal stopping of the compressor is avoided, and the compressor is protected; and when the compressor enters an internal circulation mode, the variable-frequency low-energy-consumption operation is carried out.
Specifically, referring to fig. 2, the gas source 1 is a hydrogen long Tube Trailer (TT) provided with a main outlet valve. The outlet main valve of the hydrogen pipe trailer (TT) is connected with the first pipeline 11 through a first hose 61. And a manual valve HNV-101 is arranged between the first hose 61 and the first pressure gauge PIT-101 and is used for manually opening an air path between the first hose 61 and the air filling pipeline system. The first pressure gauge PIT-101 comprises a pressure gauge valve HNV-102, the second pressure gauge PIT-102 comprises a pressure gauge valve HNV-107, the first pressure gauge PIT-101 and the second pressure gauge PIT-102 are remote pressure gauges and are electrically connected with the controller, and when the pressure gauge is used, the corresponding pressure gauge valve needs to be opened. The outlet end of the first pressure gauge PIT-101 is also connected with a site pressure gauge PG-101 (not shown in the figure), and the outlet end of the second pressure gauge PIT-102 is also connected with a site pressure gauge PG102 for displaying the site pressure value; the gas flowmeter FIQ-101 is used for detecting the gas flow, and the field pressure gauge PG102 comprises a manual valve HNV-108 which is used for opening a detection pipeline of the field pressure gauge PG 102.
Further, referring to FIG. 3, the replacement piping system includes an inert gas source 200, such as nitrogen stored in a nitrogen cylinder, and replacement piping connecting the nitrogen gas source to the gas supply piping system. The replacement pipeline comprises a first replacement pipeline 21 connected with the outlet end of the nitrogen gas source and the inlet end of the first pressure gauge PIT-101, and a second replacement pipeline 22 connected with the outlet end of the nitrogen gas source and the inlet end of the third pneumatic valve PBV-103, wherein the first replacement pipeline 21 and the second replacement pipeline 22 are used for replacing air in the gas supply pipeline system with nitrogen. The first replacement pipeline 21 is provided with a first stop valve HNV-124 for opening the gas circuit of the first replacement pipeline 21 and the gas charging pipeline system, so that nitrogen gas enters the gas charging pipeline system. The second replacement pipeline 22 is provided with a second stop valve HNV-117 for opening the gas circuit of the second replacement pipeline 22 and the gas filling pipeline system, so that nitrogen enters the gas filling pipeline system. Specifically, the nitrogen steel cylinder comprises an outlet valve, the rear end of the outlet valve of the nitrogen steel cylinder is connected with a manual nitrogen outlet valve HNV-119 for opening a gas path of the replacement pipeline, and the outlet end of the manual nitrogen outlet valve HNV-119 is further connected with a pressure regulating valve for regulating the outlet pressure of the nitrogen steel cylinder.
Further, the evacuation piping system is used for evacuating and depressurizing the gas in the gas supply piping system during inert gas replacement or hydrogenation, and specifically comprises: a first vent pipe 31 connected with the outlet end of the first pressure gauge PIT-101, a second vent pipe 32 connected with the outlet end of the compressor 40, and a third vent pipe 33 connected with the outlet end of the second pressure gauge PIT-102; the first emptying pipe 31 is provided with a first emptying valve HNV-103 for opening the first emptying pipe 31 for emptying and pressure relief; the second emptying pipe 32 is provided with a second emptying valve HNV-115 for opening the second emptying pipe 32 for emptying and pressure relief; the third emptying pipe 33 is provided with a third emptying valve HNV-109 for opening the third emptying pipe 33 to empty and release pressure. The first, second and third venting pipes 31, 32, 33 merge into a venting manifold.
Further, a bypass valve HNV-116 is further disposed on the first pipeline 11 and used for manually opening the air path of the first pipeline 11 to enable the air to carry out hydrogen serial connection through the first pipeline 11, and the bypass valve HNV-116 is disposed between the first pneumatic valve PBV-101 and the third pneumatic valve PBV-103. An inlet valve HNV-104 is further arranged at the inlet end of the compressor 40, an outlet valve HNV-105 is further arranged at the outlet end of the compressor 40, and a manual plug valve HNV-106 is arranged at the inlet end of the third pneumatic valve PBV-103.
The air gun 2 of the present example includes a hydrogenation gun model TK16 and a hydrogenation gun model TK 25. The hydrogenation gun 2-1 and the hydrogenation gun 2-2 are respectively connected and communicated with the first pipeline 11 through a second hose 62. The front end of the second hose 62 of the hydrogenation gun 2-1 on the first pipeline 11 is also provided with a manual stop valve HNV-113 for opening the gas circuit and a manual exhaust valve HNV-114 for exhausting. The front end of the second hydrogenation hose 62 of the hydrogenation gun 2-2 is also provided with a manual stop valve HNV-111 for opening the gas circuit and a manual exhaust valve HNV-112 for exhausting. An inflation main valve HNV-110 is further arranged between the manual stop valve HNV-111 and the third emptying valve 33, and a check valve is arranged at the rear ends of the manual exhaust valve HNV-114 and the manual exhaust valve HNV-112 to prevent gas backflow. And the outlet ends of the manual exhaust valve HNV-114 and the manual exhaust valve HNV-112 are respectively connected to the inlet end of a third emptying valve HNV-109.
Further, the safety monitoring system includes: the gas probe, the flame probe and the alarm are respectively and electrically connected with a controller of the control system. In this embodiment, the gas probe is a hydrogen probe.
Setting alarm concentration values of the hydrogen probe to be 10% LEL and 25% LEL respectively, sending an electric signal to the controller when detecting that an actual value is larger than 10% LEL and smaller than 25% LEL, triggering hydrogen alarm, and controlling the alarm to send an alarm prompt by the controller according to the size of the received electric signal. When the actual value is detected to be larger than 25% LEL, an electric signal is sent to the controller, the controller controls the alarm to give an alarm according to the received signal, meanwhile, the first pneumatic valve PBV-101, the second pneumatic valve PBV-102 and the third pneumatic valve PBV-103 are closed, and the control system is automatically stopped.
In the embodiment, the highest pressure alarm value of the first pressure gauge PIT-101 is set to be 25MPa, the highest pressure alarm value of the second pressure gauge PIT-102 is set to be 37MPa, when the actual pressure value of the first pressure gauge PIT-101 exceeds 25MPa or when the actual pressure value of the second pressure gauge PIT-101 exceeds 37MPa, an electric signal is sent to the controller to trigger pressure alarm, and the controller controls the alarm to send out an alarm prompt according to the received electric signal.
When alarming, the man-machine exchange interface can display alarm information. The pressure alarm may be improper valve operation or a compressor pressure protection failure. Hydrogen alarms are the result of leaks in pipes, valves, pieces, requiring equipment to be secured, or checking if other area leaks drift to it. The flame alarm will alarm when there is open fire in the scene.
In this embodiment, the controller includes an in-situ operation box, the in-situ operation box is provided with an in-situ knob, the in-situ knob includes an emergency stop switch and a knob switch, and the emergency stop switch and the knob switch are respectively electrically connected with the controller. The knob switch is used for controlling the compressor to enter a frequency conversion internal circulation state and waking up the compressor to enter a hydrogenation state, and the compressor normally works in the hydrogenation state. The knob switch comprises a bypass position and a hydrogenation position, when the knob switch is turned to the hydrogenation position, the compressor enters a hydrogenation state, when the pressure of a second pressure gauge PIT-102 rises to 35MPa, the controller controls the second pneumatic valve PBV-102 to be automatically turned on, the third pneumatic valve PBV-103 is automatically turned off, at the moment, hydrogenation is finished, the knob switch is turned to the bypass position, at the moment, the compressor 40 enters an internal circulation state, and hydrogen circulates between the compressor and the second pipeline 12. When a subsequent vehicle is hydrogenated, the compressor is hydrogenated when the knob switch is required to be turned to the hydrogenation position.
The emergency stop switch is electrically connected with the controller, when the emergency stop switch is pressed down, an electric signal is sent to the controller, and the controller controls the first pneumatic valve PBV-101, the second pneumatic valve PBV-102 and the third pneumatic valve PBV-103 to be closed according to the received electric signal. To ensure system safety, a second emergency stop switch or more emergency stop switches may be provided on site at the gas station, such as on the electrical cabinet, and on the compressor for emergency shutdown of the gas filling system.
In the embodiment, each of the first pneumatic valve PBV-101, the second pneumatic valve PBV-102 and the third pneumatic valve PBV-103 comprises a manual switch, and the states of the three pneumatic valves are switched to manual states through a man-machine exchange interface of the controller, so that the first pneumatic valve PBV-101, the second pneumatic valve PBV-102 and the third pneumatic valve PBV-103 can be manually opened and closed.
In the embodiment, the controller is a PLC controller with the model number of 6ES 7288-1 ST20-0AA 0. The model of a first pressure gauge PIT-101 is EJA530E-JBS4N-017DL/NF 2Z; the model of the second pressure gauge PIT-101 is EJX630A-EDS4N-017DL/NF 2/A1/Z. The first pressure gauge PIT-101 and the second pressure gauge PIT-101 are respectively and electrically connected with the controller, can convert pressure signals into electric signals and feed back the electric signals to the controller. The compressor is a diaphragm compressor, model number D166LM 45. The flame probe is a red ultraviolet composite flame-proof type flame detector, and the model is JTGB-HZW-BK53ExIR 2/UV. The hydrogen probe is specifically a hydrogen leakage detector, and the model is AEC2232bX, and the measuring range is: 0-100% LEL. The first pneumatic valve PBV-101 is an SBV120H2-S6+ pneumatic actuator; the second pneumatic valve PBV-102 and the third pneumatic valve PBV-103 are model SBV120H2-S6+ pneumatic actuators. It should be noted that the types of these components are not used to limit the protection scope of the present invention, and the specific types may be adjusted according to the needs of the actual hydrogen filling station, and are not described herein again.
Example 2
This embodiment provides a filling method of the gas filling system of embodiment 1. The method comprises the following steps: nitrogen displacement, hydrogen displacement and hydrogenation.
Before nitrogen replacement, firstly, a hydrogen long pipe trailer (TT) hose, a compressor 40, a hydrogenation panel, a hydrogenation gun hose and a nitrogen bottle hose are connected and fastened, a hydrogenation gun is driven to an OFF position, and a gun head cannot point to people and equipment. The various line valves of the gas filling system are checked in order to keep each valve closed.
Nitrogen replacement:
(1) the first stage pipeline is replaced by purging, and the first stage pipeline refers to a pipeline from an outlet main valve of a hydrogen long-pipe trailer (TT) to an inlet end of the first emptying pipe 31.
Specifically, a first stop valve HNV-124 on the first replacement pipeline 21, a manual valve HNV-101 on the first pipeline 11, a pressure gauge valve of a field pressure gauge PG-101 and a pressure gauge valve HNV-102 of the first pressure gauge are sequentially opened, an outlet valve of the nitrogen steel cylinder is opened, a nitrogen outlet valve HNV-119 is opened, a pressure regulating valve is adjusted to enable the pressure to be 0.5MPa, when the pressure of a pipeline is indicated to reach 0.5MPa by the first pressure gauge PIT-101, the nitrogen outlet valve HNV-119 is closed, and nitrogen charging is stopped. And then opening a first emptying valve HNV-103 on the first emptying pipe 31, decompressing the first section of pipeline, and closing the first emptying valve HNV-103 when the pressure of the pipeline is reduced to 0.05 MPa. In accordance with this method, the first stage of the line was replaced 5 times in a repeated manner.
(2) And a second section of pipeline purging replacement, wherein the second section of pipeline refers to a pipeline from the first pneumatic valve PBV-101 to the third pneumatic valve PBV-103, and comprises a part of the pipeline of the first pipeline 11, the second pipeline 12 and pipelines at the inlet end and the outlet end of the compressor.
Specifically, firstly, the valve state is ensured, the first stop valve HNV-124 on the first replacement pipeline 21, the pressure gauge valve HNV-102 of the first pressure gauge, the pressure gauge valve of the on-site pressure gauge PG-101, the first pneumatic valve PBV-101, the inlet valve HNV-104 of the compressor, the outlet valve HNV-105 of the compressor, the bypass valve HNV-116 and the second pneumatic valve PBV-102 are in an open state, and the rest valves are all closed. And opening an outlet valve of the nitrogen steel cylinder, opening a nitrogen outlet valve HNV-119, adjusting the pressure regulating valve to enable the pressure to be 0.5MPa, and closing the nitrogen outlet valve HNV-119 and stopping filling nitrogen when the first pressure gauge PIT-101 indicates that the pressure of the pipeline reaches 0.5 MPa. And then opening a second emptying valve HNV-115 on the second emptying pipe 32, depressurizing the second section of pipeline, and closing the second emptying valve HNV-115 when the pressure of the pipeline is reduced to 0.05 MPa. In accordance with this method, the second stage of the line was replaced 5 times in a repeated manner.
(3) And purging and replacing a third pipeline, wherein the third pipeline refers to a pipeline between the rear end of the third pneumatic valve PBV-103 and the air gun 2.
And confirming the state of the valves, wherein a second stop valve HNV-117, a manual plug valve HNV-106, a third pneumatic valve PBV-103, a pressure gauge valve HNV-107 of a second pressure gauge, a pressure gauge valve of a field pressure gauge PG-101, HNV-108, a main inflation valve HNV-110, a manual inflation valve HNV-111 and a manual inflation valve HNV-113 on the second replacement pipeline 22 are in an open state, TK16 type hydrogenation guns and TK25 type hydrogenation guns are in an OFF position, and other valves are in a closed state. And opening an outlet valve of the nitrogen steel cylinder, opening a nitrogen outlet valve HNV-119, adjusting the pressure regulating valve to enable the pressure to be 0.5MPa, and closing the nitrogen outlet valve HNV-119 and stopping filling nitrogen when a second pressure gauge PIT-102 indicates that the pressure of the pipeline reaches 0.5 MPa. And then opening a third emptying valve HNV-109 on the third emptying pipe 33, depressurizing the third section of pipeline, and closing the valve HNV-109 when the pressure of the pipeline is reduced to 0.05 MPa.
According to this method, the third section of pipeline was replaced 5 times (note that the last few times of pressure relief were performed through the manual vent valve HNV-112, the manual vent valve HNV-114, ensuring that the slight positive pressure nitrogen was filled between the HNV-112, HNV-114 valves and the check valve.
At this point, the replacement of air by nitrogen is completed and all valves of the system (including the outlet valve of the nitrogen cylinder) are closed. The outlet end of the pressure gauge of the nitrogen steel cylinder is also connected with a nitrogen vent pipe, and the nitrogen vent pipe is provided with a nitrogen vent valve HNV-120. The HNV-120 valve is closed by opening the HNV-120 to relieve the pressure of the outlet pipeline of the nitrogen cylinder until the pressure gauge indicates 0 (micro positive pressure).
The explosion limit of hydrogen in air is 4% -75%, and above or below the limit, the hydrogen cannot explode. And (3) replacing nitrogen before hydrogenation, namely replacing air in the gas filling pipeline system with nitrogen, so that the purity of hydrogen in the gas filling pipeline system is ensured, the possibility of hydrogen explosion is reduced, and the safety of a gas filling system is ensured. And the first section pipeline, the second section pipeline and the third section pipeline are respectively subjected to purging replacement, so that the air content in the gas supply pipeline system is further reduced, and the purity of hydrogen in the gas supply pipeline system is ensured.
In this embodiment, nitrogen replacement of the gas supply pipeline system, specifically, the division of the first section of pipeline, the second section of pipeline, and the third section of pipeline is not used to limit the protection scope of the present invention, and the division may be performed according to the actual pipeline length and the position of the valve, so as to complete nitrogen replacement, which is not described in detail herein.
(II) replacement by Hydrogen
(1) After the nitrogen replacement is finished, firstly ensuring that all valves of the system are in a closed state; then, opening a manual valve HNV-101 of the gas filling pipeline system, a pressure gauge valve HNV-102 of a first pressure gauge, a pressure gauge valve of a field pressure gauge PG-101, a first pneumatic valve PBV-101, an inlet valve HNV-104 of a compressor, an outlet valve HNV-105 of the compressor, a bypass valve HNV-116, a second pneumatic valve PBV-102, a manual plug valve HNV-106, a third pneumatic valve PBV-103, a second stop valve HNV-107, an HNV-108, a main inflation valve HNV-110, a manual inflation valve HNV-111 and a manual inflation valve HNV-113; the hydrogenation gun is OFF.
Slowly open the outlet valve of a certain fish detonator of hydrogen long Tube Trailer (TT) after, slowly open hydrogen long tube trailer export main valve (the hydrogen long tube trailer that has the emergency cut-off valve, open the emergency cut-off valve earlier), pressurize gas supply pipeline system, when first manometer PI-101 rose to 10MPa, close hydrogen long tube trailer export main valve, to each valve and the joint of pipeline, the joint department of instrument and pipeline with examine leakage liquid and hydrogen detector leak hunting.
(2) After the leakage detection is finished, the third vent valve HNV-109 is slowly opened to vent the pipeline, and the opening degree of the vent valve is not too large (noise, flammable and explosive gas).
If the joint has leakage, the leakage part is fastened again after the gas in the pipeline is discharged, and the leakage is detected again until no leakage exists.
If the joint is not leaked, when the pressure gauge is discharged to the site and displays 0.5MPa, the gas filling pipeline system is replaced for 5 times by operating the main valve of the outlet of the hydrogen long pipe trailer and the third emptying valve HNV-109, and then the positive pressure in the hose is kept for waiting for a hydrogenation notice.
The hydrogen replacement can further ensure the purity of the hydrogen filled into the vehicle to be filled, reduce the explosion risk of the hydrogen, and simultaneously leak the pipeline system, reduce the possibility of gas leakage, ensure the safety of the gas filling system and avoid potential safety hazards caused by hydrogen leakage.
(III) hydroprocessing
(1) Inspection before hydrogenation
1) Checking the pipeline valve open-close state: and opening valves HNV-101, HNV-102 and a pressure gauge valve of a field pressure gauge PG-101 of the gas supply pipeline system, HNV-104, HNV-105, HNV-116, HNV-106, HNV-107, HNV-108, HNV-110, HNV-111 and HNV-113, turning OFF a hydrogenation gun, and closing other valves.
2) After the vehicle to be filled stops at the designated position, the driver extinguishes, the vehicle leaves the hydrogenation area after static electricity is released, and hydrogenation personnel place a vehicle blocking notice board at the tail of the vehicle to be filled, place a wheel block and carry out static electricity grounding on the vehicle.
3) And (3) confirming the type of the gas cylinder interface of the vehicle to be filled by the hydrogenator, checking the effective date and the residual pressure of the gas cylinder, and refusing to execute the filling operation by the hydrogenator if the pressure is lower than 2MPa or the gas cylinder exceeds the effective period.
4) If the hydrogenation condition is met, butting the gun head of the hydrogenation gun with the joint of the vehicle to be filled, and rotating the hydrogenation gun 180 degrees to point to an ON position;
5) slowly opening a main valve at the outlet of the hydrogen long tube trailer;
6) referring to fig. 4, pneumatic valves PBV-101 and PBV-103 are started, PBV-102 is closed, hydrogen stringing is performed through the first pipeline 11, at the moment, the pressure of the hydrogen long-tube trailer is at a high value, and hydrogen stringing is directly completed through pressure difference; after the pressure of the hydrogen long-tube trailer is balanced with the pressure of the gas cylinder of the vehicle to be filled, an operator manually starts the compressor 40 to boost the pressure, and when the pressure of the PIT-102 is increased to indicate that the hydrogen after the pressure of the compressor is boosted comes, the bypass valve HNV116 is closed. At the moment, only the compressor charges hydrogen into the vehicle, the PIT-102 continuously rises until the pressure reaches 35MPa, the controller controls the PBV-102 to be automatically opened, and the PBV-103 is automatically closed. And after the hydrogenation of the vehicle is finished, the knob switch is turned to a bypass position, and the compressor enters the internal circulation at the moment.
At the moment, the compressor 40 is in an internal circulation state (PBV-103 is closed, PBV-101 and PBV-102 are opened), when a subsequent vehicle hydrogenates, as the pressure of the first pressure gauge PIT-102 is less than 30MPa, PBV-103 is automatically opened, PBV-102 is automatically closed, the knob switch is turned to the hydrogenation position, the manual bypass valve HNV116 can be simultaneously opened for hydrogen string at the moment, and when PIT-102 is boosted to be balanced with the pressure of PIT-101, hydrogen string is completed, and the manual bypass valve HNV116 is closed. PIT-102 continues to increase to 35MPa, the vehicle is full, PBV-102 is automatically opened, PBV-103 is automatically closed, and the vehicle is removed and the rotary switch is turned to the bypass position. The subsequent hydrogenation process of the vehicle repeats the process according to the above steps until the emergency stop switch is closed and the equipment is completely stopped.
When the hydrogenation is finished, the controller controls the third pneumatic valve PBV-103 to be automatically closed and the second pneumatic valve to be automatically opened, so that gas circulates between the compressor and the second pipeline 12, the compressor enters an internal circulation mode, the compressor does not need to be repeatedly opened and closed, the damage to the compressor caused by the normal opening and the normal stopping of the compressor is avoided, and the compressor is protected; meanwhile, when the compressor enters an internal circulation mode, the variable-frequency low-energy-consumption operation is carried out, and the energy consumption of the system operation is reduced.
In the embodiment, the hydrogenation speed of the air gun 2 is adjusted and controlled by controlling the opening degrees of the HNV-111 and the HNV-113 according to the sound of the air flow and the rising condition of the vehicle-mounted pressure gauge of the vehicle to be filled, and the hydrogenation speed is not too high.
In the embodiment, if the hydrogenation frequency of the vehicle to be filled is high, the gas in the hose does not need to be discharged, the compressor does not need to be stopped, and the positive pressure of the pipeline is kept. If the hydrogenation frequency is too low (less than or equal to 3 times/day), the compressor is stopped, the emergency stop switch is closed, the gas in the second hose 62 is discharged through the HNV-112 and HNV-114 valves, and nitrogen replacement and hydrogen replacement are carried out again when the next hydrogenation operation is carried out.
In the embodiment, when the hydrogen long-tube trailer is shut down for a long time, the outlet main valve of the hydrogen long-tube trailer is closed, the hydrogenation gun is in an OFF instruction, the emergency stop switch is closed, the emptying valves HNV-103, HNV-115 and HNV-109 are slowly opened to empty and release the pipelines, and all the valves are closed.
In this embodiment, in order to guarantee the high-efficient utilization of hydrogen long-tube trailer, when hydrogenation operation, recommend single fish detonator to use in proper order.
The foregoing disclosure discloses only the preferred embodiments of the invention. The preferred embodiments are not intended to be exhaustive or to limit the invention to the precise embodiments disclosed. Obviously, many modifications and variations are possible in light of the above teaching. The embodiments were chosen and described in order to best explain the principles of the invention and the practical application, to thereby enable others skilled in the art to best utilize the invention. The invention is limited only by the claims and their full scope and equivalents.

Claims (10)

1. A gas filling system is characterized by comprising a gas source, a pipeline system and a control system; wherein the content of the first and second substances,
the pipeline system comprises an air charging pipeline system, a replacement pipeline system and an emptying pipeline system; the air filling pipeline system comprises a first pipeline for connecting the air source with a vehicle to be filled, the first pipeline is provided with a first pressure gauge and a first pneumatic valve, the first pressure gauge is used for detecting air pressure, the inlet end of the first pressure gauge is connected with the outlet of the air source, and the outlet end of the first pressure gauge is connected with the inlet end of the first pneumatic valve; the rear end of the first pneumatic valve is also provided with a third pneumatic valve and a second pressure gauge, the outlet end of the first pneumatic valve is connected with the inlet end of the third pneumatic valve, the outlet end of the third pneumatic valve is connected with the second pressure gauge, and the outlet end of the second pressure gauge is connected with at least one air gun;
the outlet end of the first pneumatic valve is also connected with a compressor, and the outlet end of the compressor is connected with the inlet end of the third pneumatic valve; the gas adding pipeline system also comprises a second pipeline, the second pipeline is connected with the inlet end of the compressor and the outlet end of the compressor, and the second pipeline is provided with a second pneumatic valve;
the control system comprises a safety monitoring system and an electrical control system; the electric control system comprises a controller and a man-machine exchange interface, the controller is respectively electrically connected with the first pneumatic valve, the second pressure gauge and the third pneumatic valve, and the controller controls the first pneumatic valve, the second pressure gauge and the third pneumatic valve to be opened and closed.
2. The gas filling system of claim 1,
the replacement pipeline system comprises an inert gas source and a replacement pipeline which is connected with the inert gas source and the gas adding pipeline system; the replacement pipeline comprises a first replacement pipeline and a second replacement pipeline, wherein the first replacement pipeline is connected with the outlet end of the inert gas source and the inlet end of the first pressure gauge, and the second replacement pipeline is connected with the outlet end of the inert gas source and the inlet end of the third pneumatic valve; the first replacement pipeline is provided with a first stop valve, and the second replacement pipeline is provided with a second stop valve;
the emptying pipeline system comprises: a first vent pipe connected with the outlet end of the first pressure gauge, a second vent pipe connected with the outlet end of the compressor, and a third vent pipe connected with the outlet end of the second pressure gauge; the first emptying pipe is provided with a first emptying valve, the second emptying pipe is provided with a second emptying valve, and the third emptying pipe is provided with a third emptying valve.
3. The gas filling system of claim 2, wherein the safety monitoring system comprises: the gas probe, the flame probe and the alarm are respectively and electrically connected with a controller of the control system.
4. A gas filling system according to claim 3, wherein the gas source is a hydrogen tube trailer having a gas source pressure of 15-20 MPa.
5. A gas filling method, characterized by using the gas filling system according to claim 4, comprising the steps of:
(1) performing inert gas replacement on the gas adding pipeline system, and replacing air in the gas adding pipeline system with inert gas;
(2) replacing the gas to be inflated in the gas filling pipeline system, replacing inert gas in the gas filling pipeline system with the gas to be inflated, and checking gas leakage of the gas filling pipeline system;
(3) safety inspection before gas filling is carried out, open fire and fire operation around the gas filling process are ensured, and static grounding is carried out on the vehicle to be filled;
(4) and filling gas into the vehicle to be filled, and after filling gas, closing the third pneumatic valve and opening the second pneumatic valve to enable the gas to circulate between the compressor and the second pipeline.
6. The gas filling method according to claim 5, wherein in the hydrogenation step, when the gas cylinder pressure of the vehicle to be filled is lower than the gas source pressure, the vehicle to be filled is filled with gas through the first pipeline, and when the gas cylinder pressure of the vehicle to be filled is balanced with the gas source pressure, the compressor is started, and the vehicle to be filled is filled with gas through the compressor.
7. The gas filling method according to claim 5, wherein, during hydrogenation, a gas source is used for filling gas through the first pipeline and the compressor is started to fill gas into the vehicle to be filled.
8. The gas filling method according to claim 5, wherein the alarm threshold of the first pressure gauge is set to 25MPa, the alarm threshold of the second pressure gauge is set to 37MPa, and the alarm threshold of the hydrogen probe is set to 10% LEL.
9. The gas filling method according to claim 5, wherein the compressor is electrically connected to the controller, and the controller includes a knob switch, and the compressor is controlled to enter the internal circulation state or the gas filling state by operating the knob switch.
10. The gas filling method according to claim 5, wherein the step (1) includes: opening the first replacement pipeline to fill inert gas into the first section of pipeline, stopping filling the inert gas when the pressure indicated by a first pressure gauge reaches 0.5MPa, opening the first emptying valve, and performing pressure relief through the first emptying pipeline; opening the first replacement pipeline to fill inert gas into the second section of pipeline, stopping filling the inert gas when the pressure indicated by the first pressure gauge reaches 0.5MPa, opening the second emptying valve, and performing pressure relief through the second emptying pipeline; and opening the third replacement pipeline to fill inert gas into the third section of pipeline, stopping filling the inert gas when the pressure indicated by the second pressure gauge reaches 0.5MPa, opening the third emptying valve, and performing pressure relief through the third emptying pipeline to complete inert gas replacement of the gas adding pipeline system.
CN201911294012.9A 2019-12-16 2019-12-16 Gas filling system and filling method Pending CN110985881A (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111473249A (en) * 2020-05-26 2020-07-31 广东国联氢能技术有限公司 Hydrogenation system and hydrogenation control method
CN113623170A (en) * 2021-08-13 2021-11-09 上海氢枫能源技术有限公司 Compressor hydrogen circulation method and system
CN113685724A (en) * 2021-09-09 2021-11-23 天合光能(宿迁)光电有限公司 Preparation method for controlling silane on-line
CN114087527A (en) * 2021-09-26 2022-02-25 浙江浙能航天氢能技术有限公司 Control method of hydrogen filling station
CN114087526A (en) * 2021-09-26 2022-02-25 浙江浙能航天氢能技术有限公司 Control method of hydrogenation station
CN114763877A (en) * 2021-01-11 2022-07-19 神华氢能科技如皋有限责任公司 Gas filling method, control device, storage medium, and gas filling system
CN114811417A (en) * 2022-04-22 2022-07-29 武汉中极氢能源发展有限公司 Prevent hydrogenation rifle for hydrogenation station of static
CN115127013A (en) * 2021-03-25 2022-09-30 上海氢枫能源技术有限公司 Skid-mounted type pressurization hydrogenation station system and hydrogenation method thereof
CN115479208A (en) * 2022-09-16 2022-12-16 上海氢枫能源技术有限公司 Hydrogen supply system and method for long-tube trailer

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CN101418908A (en) * 2008-11-28 2009-04-29 同济大学 Air entraining system for high-pressure hydrogenation stations
CN103178277A (en) * 2011-12-22 2013-06-26 上海汽车集团股份有限公司 Full-automatic gas displacement system and method
DK201770361A1 (en) * 2017-05-22 2018-04-23 Nel Hydrogen As Method of refueling a hydrogen vehicle
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111473249A (en) * 2020-05-26 2020-07-31 广东国联氢能技术有限公司 Hydrogenation system and hydrogenation control method
CN114763877A (en) * 2021-01-11 2022-07-19 神华氢能科技如皋有限责任公司 Gas filling method, control device, storage medium, and gas filling system
CN114763877B (en) * 2021-01-11 2024-01-02 神华氢能科技如皋有限责任公司 Gas filling method, control device, storage medium and gas filling system
CN115127013A (en) * 2021-03-25 2022-09-30 上海氢枫能源技术有限公司 Skid-mounted type pressurization hydrogenation station system and hydrogenation method thereof
CN113623170A (en) * 2021-08-13 2021-11-09 上海氢枫能源技术有限公司 Compressor hydrogen circulation method and system
CN113623170B (en) * 2021-08-13 2022-12-27 上海氢枫能源技术有限公司 Compressor hydrogen circulation method and system
CN113685724A (en) * 2021-09-09 2021-11-23 天合光能(宿迁)光电有限公司 Preparation method for controlling silane on-line
CN114087527A (en) * 2021-09-26 2022-02-25 浙江浙能航天氢能技术有限公司 Control method of hydrogen filling station
CN114087526A (en) * 2021-09-26 2022-02-25 浙江浙能航天氢能技术有限公司 Control method of hydrogenation station
CN114811417A (en) * 2022-04-22 2022-07-29 武汉中极氢能源发展有限公司 Prevent hydrogenation rifle for hydrogenation station of static
CN114811417B (en) * 2022-04-22 2024-04-16 武汉中极氢能源发展有限公司 Antistatic hydrogenation gun for hydrogenation station
CN115479208A (en) * 2022-09-16 2022-12-16 上海氢枫能源技术有限公司 Hydrogen supply system and method for long-tube trailer

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