CN112856218B - Automatic flow control and protection method based on liquid oxygen flow regulation - Google Patents

Automatic flow control and protection method based on liquid oxygen flow regulation Download PDF

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Publication number
CN112856218B
CN112856218B CN202011565980.1A CN202011565980A CN112856218B CN 112856218 B CN112856218 B CN 112856218B CN 202011565980 A CN202011565980 A CN 202011565980A CN 112856218 B CN112856218 B CN 112856218B
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pressure
pressurization
valve
constant pressure
plc
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CN112856218A (en
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史向前
郭洪业
关英海
李俊杰
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Beijing Power Machinery Institute
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Beijing Power Machinery Institute
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C5/00Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/002Automated filling apparatus
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16KVALVES; TAPS; COCKS; ACTUATING-FLOATS; DEVICES FOR VENTING OR AERATING
    • F16K31/00Actuating devices; Operating means; Releasing devices
    • F16K31/02Actuating devices; Operating means; Releasing devices electric; magnetic
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/02Special adaptations of indicating, measuring, or monitoring equipment
    • F17C13/025Special adaptations of indicating, measuring, or monitoring equipment having the pressure as the parameter
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/04Arrangement or mounting of valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C5/00Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/02Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/03Control means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04Indicating or measuring of parameters as input values
    • F17C2250/0404Parameters indicated or measured
    • F17C2250/043Pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/07Actions triggered by measured parameters
    • F17C2250/072Action when predefined value is reached

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  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Control Of Fluid Pressure (AREA)

Abstract

The invention discloses an automatic flow control and protection method based on liquid oxygen flow adjustment, wherein the control system comprises: the device comprises a valve, a sensor, an upper computer and a lower computer; the upper computer exchanges data with the lower computer; the lower computer is electrically connected with the valve and the sensor respectively so as to transmit and control data; the upper computer is used for realizing man-machine exchange, a control unit of the upper computer is provided with automatic process operation software of a constant pressure valve, and an operation interface of the software is provided with a function button; when an operator selects a function button through the operation interface of the software, the control unit sends a control instruction corresponding to the function button to a lower computer; the invention can realize multiple optional, automatic pressurization, controllable stride, real-time judgment and in-place valve protection measures of the pressurization pipeline through a program, can save the operation time, improve the operation efficiency, is simple, convenient and intelligent, and provides guarantee for the liquid oxygen pressurization system.

Description

Automatic flow control and protection method based on liquid oxygen flow regulation
Technical Field
The invention belongs to the technical field of flow regulation, and particularly relates to automatic flow control and a protection method thereof based on liquid oxygen flow regulation.
Background
In order to meet the requirement of a certain high enthalpy test facility on oxygen flow in each test state, oxygen consumed by a direct combustion heater is supplemented, the molar content of oxygen in a high enthalpy working medium is ensured to be consistent with that of air, a liquid oxygen supply system adopts a nitrogen extrusion mode, 4 parts of completely same supply units form a test bed to supply liquid oxygen with stable pressure and stable flow, and precooling processes before a test and blowing-off work after the test are completed. The main component of the liquid oxygen supply system is a constant pressure valve. Whether the constant pressure valve can normally work according to requirements or not is a key step of whole system debugging and connection in relation to whether a liquid oxygen supply system can provide oxygen with corresponding flow for experimental facilities or not, the consideration is that the boost pressure is higher, the valve circulation capacity is larger, the number of boost pipelines is more, the four-way boost manual operation is more complicated, the system operation is safe and the like, and higher requirements are provided for the automatic control of the constant pressure valve.
Disclosure of Invention
In view of the above, the invention provides an automatic flow control and protection method based on liquid oxygen flow adjustment, which can realize multiple optional, automatic pressurization, controllable stride, real-time judgment and in-place valve protection measures of a pressurization pipeline through a program, save operation time, improve operation efficiency, be simple, convenient and intelligent, and provide guarantee for a liquid oxygen pressurization system.
The invention is realized by the following technical scheme:
an automatic process control system based on liquid oxygen flow regulation, comprising: valves and sensors; the valve and the sensor are respectively arranged on a pressure increasing pipeline between a nitrogen source of the liquid oxygen supply system and the liquid oxygen tank, and the valve comprises: a constant pressure valve and a pressure-increasing cutoff valve; the sensor includes: pressure sensor a and pressure sensor C; the constant pressure valve is positioned at the side of the nitrogen source, and the pressure-increasing cut-off valve is positioned at the side of the liquid oxygen tank; the pressure sensor A is positioned between the constant pressure valve and the pressure-boosting cut-off valve, and the pressure sensor C is positioned between the pressure-boosting cut-off valve and the liquid oxygen tank; the constant pressure valve is used for controlling the pressure in the pressurization pipeline to be a set value, and the pressurization cut-off valve is used for controlling the flow of a medium in the pressurization pipeline; the pressure sensor is used for detecting the pressure in the pressurization pipeline;
further comprising: an upper computer and a lower computer;
data exchange is carried out between the upper computer and the lower computer;
the lower computer is electrically connected with the valve and the sensor respectively so as to transmit and control data;
the upper computer is used for realizing man-machine exchange, the control unit of the upper computer is provided with automatic flow operation software of a constant pressure valve, the operation interface of the software is provided with function buttons, and the function buttons comprise: the method comprises the following steps of (1) selecting a pressurization pipeline, starting pressurization, inputting a pressurization set value, stopping pressurization and giving an alarm when the pressurization is overtime; when an operator selects a function button through the operation interface of the software, the control unit sends a control instruction corresponding to the function button to a lower computer;
the lower computer comprises: the PLC comprises a power supply module, a communication module, a digital quantity input module, a digital quantity output module, an analog quantity input module and an analog quantity output module;
the power supply module is used for supplying power to the PLC;
one end of the communication module is in data transmission with the upper computer through an industrial Ethernet, and the other end of the communication module is in data transmission with the PLC, so that data exchange between the PLC and the upper computer is realized;
the PLC is internally stored with a control program and is used for acquiring and storing feedback parameters of the valve and the sensor through a digital quantity input module and an analog quantity input module, and the feedback parameters comprise: the method comprises the following steps of (1) increasing the pressure of a switch limit signal of a cut-off valve and pressure data of a sensor, sending the feedback parameters to an upper computer, and displaying the feedback parameters on an operation interface of automatic flow operation software of a constant pressure valve of the upper computer; the PLC is also used for receiving a control instruction of the upper computer and controlling the opening and closing of the pressure-boosting cut-off valve and the opening of the constant pressure valve through the digital output module and the analog output module; the PLC is also used for setting a pressurization operation flow of the liquid oxygen supply system, namely setting the action sequence and time interval of each valve and carrying out corresponding action processing on the feedback parameters of the valves and the sensors.
Further, the digital quantity input module is used for acquiring a switch limit signal of the pressurization shut-off valve and sending the switch limit signal to the PLC;
the digital quantity output module is used for receiving a control signal of the PLC and controlling the on-off of the pressurization cut-off valve;
the analog quantity input module is used for acquiring pressure and temperature data of the sensor and sending the pressure and temperature data to the PLC;
and the analog output module is used for receiving a control signal of the PLC and controlling the opening of the constant pressure valve.
Further, the device also comprises a pressure sensor B, and the pressure sensor B is positioned between the constant pressure valve and the nitrogen source.
Further, the device also comprises a temperature sensor, wherein the temperature sensor is positioned between the pressurization stop valve and the liquid oxygen tank; the temperature sensor is used for measuring the temperature in the pressurization pipeline.
A protection method based on a liquid oxygen flow regulation automatic process control system is based on the liquid oxygen flow regulation automatic process control system, and comprises the following specific steps:
step 1, operating an operation interface of automatic flow operation software of a constant pressure valve of an upper computer by an operator, and selecting a corresponding pressure boost pipeline through a function button selected by the pressure boost pipeline;
step 2, inputting a pressurization target value by an operator through a function button of a pressurization set value input box; the upper computer sends the pressurization target value to a PLC of a lower computer, the PLC sets the constant pressure valve, the pressure of the constant pressure valve is set as the pressurization target value, and meanwhile the pressurization step length of the constant pressure valve is set as a step length set value;
step 3, an operator starts an automatic pressurization program through a function button for starting pressurization; the upper computer sends a control instruction for starting pressurization to a PLC of the lower computer, the PLC controls a constant pressure valve and a pressurization cut-off valve to be opened, and controls the pressure of the constant pressure valve to be increased by a step length set value according to each set time length A to be pressurized until the pressure is equal to the pressurization target value; enabling nitrogen of a nitrogen source to enter the liquid oxygen tank through a pressurization pipeline, increasing the pressure of the liquid oxygen tank to a set value, acquiring pressure and temperature data of a measuring point of the pressurization pipeline where a sensor is located through a PLC (programmable logic controller) in the pressurization process of the liquid oxygen tank, and judging whether the pressure of the constant pressure valve is adjusted in place or not according to the pressure and temperature data; the specific judgment process is as follows:
(1) the PLC judges whether the pressure measured by the pressure sensor A exceeds the pressurization target value of the constant pressure valve in real time, if so, the pressurization shut-off valve is closed, and the pressurization of the liquid oxygen tank is stopped; if not, continuously keeping the pressurization stop valve in an opening state;
(2) the PLC judges whether the difference between the pressure measured by the pressure sensor C and the pressure measured by the pressure sensor A is within a set range in real time, and if so, the PLC continuously keeps the pressurization shut-off valve in an open state; if the pressure of the liquid oxygen tank is not within the set range, closing the pressure-increasing stop valve and stopping the pressure increase of the liquid oxygen tank;
(3) setting the pressurization target value of the constant pressure valve to be M, the step length setting value of the constant pressure valve to be L and the initial pressure of the constant pressure valve to be P, setting the pressure setting value of the constant pressure valve after the first set time length A is pressurized to be P + L, setting the pressure setting value of the constant pressure valve after the second set time length A is pressurized to be P +2L, setting the pressure setting value of the constant pressure valve after the third set time length A is pressurized to be P +3L and …, setting the pressure setting value of the constant pressure valve after the last set time length A is pressurized to be P + nL and equal to the pressurization target value M;
the PLC judges once every set time length A and judges whether the difference between the pressure measured by the pressure sensor A and the current corresponding pressure set value is less than or equal to a step length set value L;
if the step length set value is less than or equal to L, the pressure of the constant pressure valve is normal, the PLC automatically sets a pressure set value after the pressure of the next set time length A is increased by the constant pressure valve until the pressure set value of the constant pressure valve is equal to the pressure increase target value M;
if the step length is larger than the set value L, the constant pressure valve is indicated to be abnormal in work; if the pressure measured by the pressure sensor A is not less than or equal to the set step length value L after the set time length B is set, a function button for alarming the pressurization overtime on an operation interface of automatic flow operation software of a constant pressure valve of the upper computer prompts the pressurization overtime, closes the pressurization stop valve, stops the pressurization of the liquid oxygen tank, and simultaneously checks the constant pressure valve and the pressurization pipeline; if the pressure measured by the pressure sensor A is less than or equal to the step length set value and is L after the set time length B is set, the pressure of the constant pressure valve is gradually increased to the current corresponding pressure set value, the PLC automatically sets the pressure set value after the pressure of the next set time length A is increased until the pressure set value of the constant pressure valve is equal to the pressure increase target value M;
(4) when the pressure set value of the constant pressure valve is equal to the pressurization target value, the PLC judges whether the pressure of the liquid oxygen tank meets the set value or not through the pressure measured by the pressure sensor C, if yes, the execution of the automatic pressurization program is finished, and the automatic pressurization is finished through a function button for stopping pressurization on an operation interface of automatic flow operation software of the constant pressure valve of the upper computer.
Furthermore, an operator can stop the automatic pressurization program at any time through a function button for pressurization stop on an operation interface of the automatic process operation software of the constant pressure valve.
Furthermore, an operator intervenes in the pressurization process according to the pressurization condition of the liquid oxygen tank, namely, in the pressurization process, the valve can be operated through the PLC, the automatic pressurization program is stopped, the state of the valve which is not operated is kept, namely, the constant pressure valve is normally opened, and the pressurization cutoff valve is normally closed.
Further, a pressure increase set value input box on an operation interface of the automatic process operation software of the constant pressure valve of the upper computer can be manually set, namely, the pressure set value of the constant pressure valve is manually input after each set time length A until the pressure set value is equal to the pressure increase target value.
Has the beneficial effects that: (1) the method is configured through automatic flow operation software of a constant pressure valve in an upper computer, sets parameters and trigger instructions, receives feedback signals and displays corresponding supercharging parameters in real time; the lower computer receives the instruction, executes the corresponding functional module program, protects the program to monitor in real time in the pressurizing process and feeds back signals in time; the automatic, intelligent and simple man-machine interaction of liquid oxygen flow regulation is realized, the operation is stable, the pressurization supply task of the liquid oxygen system can be well completed, the logic control of the constant pressure valve is met, and the full system test is fully guaranteed.
(2) The upper computer can send instructions and receive feedback, can flexibly configure the pressurization road and the pressurization target pressure, and display the corresponding measuring point value and the valve state in real time, and the pressurization process is clear at a glance and is convenient and simple to operate; meanwhile, the manual operation function is reserved, and the automatic pressurization program is independent and not interfered with each other, and can be switched according to the operation condition.
(3) The PLC can complete uploading and issuing of control instructions, data transmission, processing of feedback signals of the valve (namely switch limit signals of the valve), and recording of parameters such as temperature and pressure sent by the sensor; when any one feedback parameter reaches a set value, the PLC performs protection action on the liquid oxygen supply system to protect the safety of the liquid oxygen system, if an abnormal condition occurs, a protection program is started preferentially to execute corresponding process operation, and the operation risk of the pressurization system is reduced.
Drawings
FIG. 1 is a schematic diagram of the present invention;
Detailed Description
The invention is described in detail below by way of example with reference to the accompanying drawings.
Example 1:
this embodiment provides a flow control system based on liquid oxygen flow control automation, includes: the system comprises an upper computer, a lower computer, a valve and a sensor;
the valve and the sensor are respectively arranged on a pressure increasing pipeline between a nitrogen source of the liquid oxygen supply system and the liquid oxygen tank, and the valve comprises: a constant pressure valve and a pressure-increasing cutoff valve; the sensor includes: three pressure sensors and one temperature sensor; the constant pressure valve is positioned at the side of the nitrogen source, and the pressure-increasing stop valve is positioned at the side of the liquid oxygen tank; enabling the three pressure sensors to be a pressure sensor A, a pressure sensor B and a pressure sensor C respectively; the pressure sensor A is positioned between the constant pressure valve and the pressure-boosting cut-off valve, the pressure sensor B is positioned between the constant pressure valve and the nitrogen source, and the pressure sensor C is positioned between the pressure-boosting cut-off valve and the liquid oxygen tank; the temperature sensor is positioned between the pressure-increasing stop valve and the liquid oxygen tank; the constant pressure valve is used for controlling the pressure in the pressurization pipeline to be a set value, and the pressurization cut-off valve is used for controlling the flow of a medium in the pressurization pipeline; the pressure sensor is used for detecting the pressure in the pressurization pipeline, and the temperature sensor is used for measuring the temperature in the pressurization pipeline;
referring to fig. 1, the upper computer and the lower computer exchange data through an industrial ethernet;
the lower computer is electrically connected with the valve and the sensor respectively so as to transmit and control data;
the system comprises an upper computer, a control unit of the upper computer, a configuration software Labview, a constant pressure valve automatic flow operation software and a control unit of the upper computer, wherein the upper computer is used for realizing man-machine exchange, and the constant pressure valve automatic flow operation software is written by the configuration software Labview; the operation interface of software is equipped with the function button, the function button includes: the method comprises the following steps of (1) selecting a pressurization pipeline, starting pressurization, inputting a pressurization set value, stopping pressurization and giving an alarm when the pressurization is overtime; when an operator selects a function button through the operation interface of the software, the control unit sends a control instruction corresponding to the function button to a lower computer;
the lower computer comprises: the PLC comprises a power supply module, a communication module, a digital quantity input module, a digital quantity output module, an analog quantity input module and an analog quantity output module;
the power supply module is used for supplying power to the PLC;
one end of the communication module is in data transmission with the upper computer through an industrial Ethernet, and the other end of the communication module is in data transmission with the PLC, so that data exchange between the PLC and the upper computer is realized;
the PLC adopts ohm dragon series; the PLC is internally stored with a control program, the control program is written by CX-one software, and an independent program segment is provided for executing a pressurization task, and the pressurization task comprises: communication, valve control, sensor data acquisition, data processing, pressurization process setting and safety function setting; the PLC is used for acquiring and storing feedback parameters (namely, a switch limit signal of the valve and pressure and temperature data of the sensor) of the valve and the sensor through the digital input module and the analog input module, sending the feedback parameters to the upper computer, and displaying the feedback parameters on an operation interface of automatic process operation software of a constant pressure valve of the upper computer; the PLC is also used for receiving a control instruction of the upper computer and controlling the opening and closing of the valve through the digital output module and the analog output module; the PLC is also used for setting a pressurization operation flow of the liquid oxygen supply system, namely setting the action sequence and time interval of each valve and performing corresponding action processing on the feedback parameters of the valves and the sensors;
the digital quantity input module is used for acquiring a switch limit signal of the pressurization cut-off valve and sending the switch limit signal to the PLC;
the digital quantity output module is used for receiving a control signal of the PLC and controlling the on-off of the pressurization shut-off valve;
the analog input module is used for acquiring pressure and temperature data of the sensor and sending the pressure and temperature data to the PLC;
and the analog output module is used for receiving a control signal of the PLC and controlling the opening of the constant pressure valve.
Example 2:
the embodiment provides a protection method of an automatic process control system based on liquid oxygen flow regulation, which comprises the following specific steps:
step 1, operating on an operation interface of automatic process operation software of a constant pressure valve of an upper computer by an operator, and selecting a corresponding pressure boost pipeline through a function button selected by the pressure boost pipeline;
step 2, an operator inputs a supercharging target value through a function button of a supercharging set value input box; the upper computer sends the pressurization target value to a PLC of a lower computer, the PLC sets the constant pressure valve, the pressure of the constant pressure valve is set as the pressurization target value, and meanwhile the pressurization step length of the constant pressure valve is set as a step length set value;
step 3, an operator starts an automatic pressurization program through a function button for starting pressurization; the upper computer sends a control instruction for starting pressurization to a PLC of the lower computer, the PLC controls a constant pressure valve and a pressurization cut-off valve to be opened, and controls the pressure of the constant pressure valve to be increased by a step length set value every 10s until the pressure is equal to the pressurization target value; enabling nitrogen of a nitrogen source to enter the liquid oxygen tank through a pressurization pipeline, increasing the pressure of the liquid oxygen tank to a set value, acquiring pressure and temperature data of a measuring point of the pressurization pipeline where a sensor is located through a PLC (programmable logic controller) in the pressurization process of the liquid oxygen tank, and judging whether the pressure of the constant pressure valve is adjusted in place or not according to the pressure and temperature data; the specific judgment process is as follows:
(1) the PLC judges whether the pressure measured by the pressure sensor A exceeds the pressurization target value of the constant pressure valve in real time, if so, the pressurization shut-off valve is closed, and the pressurization of the liquid oxygen tank is stopped; if not, continuously keeping the pressurization stop valve in an opening state;
(2) the PLC judges whether the difference between the pressure in the liquid oxygen tank (namely the pressure measured by the pressure sensor C) and the pressure measured by the pressure sensor A is within a set range in real time, and if so, the PLC continuously keeps the pressurization shut-off valve in an open state; if the pressure of the liquid oxygen tank is not within the set range, closing the pressure-increasing stop valve and stopping the pressure increase of the liquid oxygen tank;
(3) setting the pressurization target value of the constant pressure valve as M, the step length setting value of the constant pressure valve as L and the initial pressure of the constant pressure valve as P, wherein the pressure setting value after the first 10s pressurization of the constant pressure valve is P + L, the pressure setting value after the second 10s pressurization is P +2L, the pressure setting value after the third 10s pressurization is P +3L, …, and the pressure setting value after the last 10s pressurization is P + nL and is equal to the pressurization target value M;
the PLC judges every 10s and judges whether the difference between the pressure measured by the pressure sensor A and the current corresponding pressure set value is less than or equal to a step length set value L;
if the step length set value is less than or equal to L, the pressure of the constant pressure valve is normal, the PLC automatically sets a pressure set value after the pressure of the constant pressure valve is increased for the next 10s until the pressure set value of the constant pressure valve is equal to the pressure increase target value M;
if the step length is larger than the set value L, the constant pressure valve is abnormal in work; if the pressure measured by the pressure sensor A is not less than or equal to the set step length value L after 30s, a function button for alarming the pressurization overtime on an operation interface of automatic flow operation software of the constant pressure valve of the upper computer prompts the pressurization overtime, closes the pressurization stop valve, stops the pressurization of the liquid oxygen tank, and takes measures, namely, the constant pressure valve and the pressurization pipeline are checked; if the pressure measured by the pressure sensor A is less than or equal to the step length set value and is L after 30s, the pressure of the constant pressure valve is gradually increased to the current corresponding pressure set value, the PLC automatically sets the pressure set value after the pressure of the constant pressure valve is increased for the next 10s until the pressure set value of the constant pressure valve is equal to the pressure increase target value M;
for example, in this embodiment, the target value of the pressurization of the constant pressure valve is 10MP, the step size setting value is 0.5MP, the initial pressure is OMP, the constant pressure valve performs pressurization every 10 seconds from OMP, the first pressure setting value is 0.5MP, the second pressure is 1MP, the third pressure is 1.5MP, …, and up to the pressurization of 10 MP;
if the constant pressure valve is pressurized to 3MP, the current pressure set value is 3MP, and if the pressure measured by the pressure sensor A is more than 2.5MP, the pressure is less than the step length set value by 0.5 MP; if the pressure increase is normal, the PLC automatically sets the next pressure set value to be 3.5MP to the pressure setting valve; if the pressure measured by the pressure sensor A is less than 2.5 and greater than 0.5MP, the constant pressure valve is abnormal in operation;
(4) when the pressure set value of the constant pressure valve is equal to the pressurization target value M, the PLC judges whether the pressure of the liquid oxygen tank meets the set value or not through the pressure measured by the pressure sensor C, if yes, the execution of the automatic pressurization program is finished, and the automatic pressurization is finished through a function button for stopping pressurization on an operation interface of automatic flow operation software of the constant pressure valve of the upper computer.
Wherein, the operator can stop the automatic pressurization program at any time through a function button for stopping pressurization on the operation interface of the automatic flow operation software of the constant pressure valve;
an operator can intervene in the pressurization process according to the pressurization condition of the liquid oxygen tank, namely, in the pressurization process, the valve can be operated through the PLC, the automatic pressurization program is stopped, and the state of the valve which is not operated is kept, namely, the constant pressure valve is normally opened and the pressurization cutoff valve is normally closed;
and a pressure-increasing set value input box on an operation interface of the automatic flow operation software of the constant pressure valve of the upper computer can be manually set, namely, the pressure set value of the constant pressure valve is manually input every 10s until the pressure set value is equal to a pressure-increasing target value.
In summary, the above description is only a preferred embodiment of the present invention, and is not intended to limit the scope of the present invention. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (4)

1. A protection method based on a liquid oxygen flow regulation automatic process control system is based on the liquid oxygen flow regulation automatic process control system, and the control system comprises: valves and sensors; the valve and the sensor are respectively arranged on a pressure increasing pipeline between a nitrogen source of the liquid oxygen supply system and the liquid oxygen tank, and the valve comprises: a constant pressure valve and a pressure-increasing cutoff valve; the sensor includes: pressure sensor a and pressure sensor C; the constant pressure valve is positioned at the side of the nitrogen source, and the pressure-increasing cut-off valve is positioned at the side of the liquid oxygen tank; the pressure sensor A is positioned between the constant pressure valve and the pressure-boosting cut-off valve, and the pressure sensor C is positioned between the pressure-boosting cut-off valve and the liquid oxygen tank; the constant pressure valve is used for controlling the pressure in the pressurization pipeline to be a set value, and the pressurization cut-off valve is used for controlling the flow of a medium in the pressurization pipeline; the pressure sensor is used for detecting the pressure in the pressurization pipeline;
the control system further comprises: an upper computer and a lower computer;
data exchange is carried out between the upper computer and the lower computer;
the lower computer is electrically connected with the valve and the sensor respectively so as to transmit and control data;
the upper computer is used for realizing man-machine exchange, the control unit of the upper computer is provided with automatic process operation software of a constant pressure valve, an operation interface of the software is provided with function buttons, and the function buttons comprise: the method comprises the following steps of (1) selecting a pressurization pipeline, starting pressurization, inputting a pressurization set value, stopping pressurization and giving an alarm when the pressurization is overtime; when an operator selects a function button through the operation interface of the software, the control unit sends a control instruction corresponding to the function button to a lower computer;
the lower computer comprises: the PLC comprises a power supply module, a communication module, a digital quantity input module, a digital quantity output module, an analog quantity input module and an analog quantity output module;
the power supply module is used for supplying power to the PLC;
one end of the communication module is in data transmission with the upper computer through an industrial Ethernet, and the other end of the communication module is in data transmission with the PLC, so that data exchange between the PLC and the upper computer is realized;
the PLC is internally stored with a control program and is used for acquiring and storing feedback parameters of the valve and the sensor through a digital quantity input module and an analog quantity input module, and the feedback parameters comprise: the method comprises the following steps of (1) increasing the pressure of a switch limit signal of a cut-off valve and pressure data of a sensor, sending the feedback parameters to an upper computer, and displaying the feedback parameters on an operation interface of automatic flow operation software of a constant pressure valve of the upper computer; the PLC is also used for receiving a control instruction of the upper computer and controlling the opening and closing of the pressure-boosting cut-off valve and the opening of the constant pressure valve through the digital output module and the analog output module; the PLC is also used for setting a pressurization operation flow of the liquid oxygen supply system, namely setting the action sequence and time interval of each valve and performing corresponding action processing on the feedback parameters of the valves and the sensors;
the method is characterized by comprising the following specific steps:
step 1, operating on an operation interface of automatic process operation software of a constant pressure valve of an upper computer by an operator, and selecting a corresponding pressure boost pipeline through a function button selected by the pressure boost pipeline;
step 2, an operator inputs a supercharging target value through a function button of a supercharging set value input box; the upper computer sends the pressurization target value to a PLC of a lower computer, the PLC sets the constant pressure valve, the pressure of the constant pressure valve is set as the pressurization target value, and meanwhile the pressurization step length of the constant pressure valve is set as a step length set value;
step 3, an operator starts an automatic pressurization program through a function button for starting pressurization; the upper computer sends a control instruction for starting pressurization to a PLC (programmable logic controller) of the lower computer, the PLC controls a constant pressure valve and a pressurization cutoff valve to be opened, and controls the pressure of the constant pressure valve to be increased by a step length set value according to each set duration A until the pressure is equal to the pressurization target value; enabling nitrogen of a nitrogen source to enter the liquid oxygen tank through a pressurization pipeline, increasing the pressure of the liquid oxygen tank to a set value, acquiring pressure and temperature data of a measuring point of the pressurization pipeline where a sensor is located through a PLC (programmable logic controller) in the pressurization process of the liquid oxygen tank, and judging whether the pressure of the constant pressure valve is adjusted in place or not according to the pressure and temperature data; the specific judgment process is as follows:
(1) the PLC judges whether the pressure measured by the pressure sensor A exceeds the pressurization target value of the constant pressure valve in real time, if so, the pressurization shut-off valve is closed, and the pressurization of the liquid oxygen tank is stopped; if not, continuously keeping the pressurization stop valve in an opening state;
(2) the PLC judges whether the difference between the pressure measured by the pressure sensor C and the pressure measured by the pressure sensor A is within a set range in real time, and if so, the PLC continuously keeps the pressurization shut-off valve in an open state; if the pressure of the liquid oxygen tank is not within the set range, closing the pressure-increasing stop valve and stopping the pressure increase of the liquid oxygen tank;
(3) setting the pressurization target value of the constant pressure valve to be M, the step length setting value of the constant pressure valve to be L and the initial pressure of the constant pressure valve to be P, setting the pressure setting value of the constant pressure valve after the first set time length A is pressurized to be P + L, setting the pressure setting value of the constant pressure valve after the second set time length A is pressurized to be P +2L, setting the pressure setting value of the constant pressure valve after the third set time length A is pressurized to be P +3L and …, setting the pressure setting value of the constant pressure valve after the last set time length A is pressurized to be P + nL and equal to the pressurization target value M;
the PLC judges once every set time length A and judges whether the difference between the pressure measured by the pressure sensor A and the current corresponding pressure set value is less than or equal to a step length set value L or not;
if the set value of the step length is less than or equal to L, the pressure of the constant pressure valve is normal, the PLC automatically sets the pressure set value after the pressure is increased for the next set time length A by the constant pressure valve until the pressure set value of the constant pressure valve is equal to the pressure increase target value M;
if the step length is larger than the set value L, the constant pressure valve is indicated to be abnormal in work; if the pressure measured by the pressure sensor A is not less than or equal to the set step length value L after the set time length B is set, a function button for alarming the pressurization overtime on an operation interface of automatic flow operation software of a constant pressure valve of the upper computer prompts the pressurization overtime, closes the pressurization stop valve, stops the pressurization of the liquid oxygen tank, and simultaneously checks the constant pressure valve and the pressurization pipeline; if the pressure measured by the pressure sensor A is less than or equal to the step length set value and is L after the set time length B is set, the pressure of the constant pressure valve is gradually increased to the current corresponding pressure set value, the PLC automatically sets the pressure set value after the pressure of the next set time length A is increased until the pressure set value of the constant pressure valve is equal to the pressure increase target value M;
(4) when the pressure set value of the constant pressure valve is equal to the pressurization target value, the PLC judges whether the pressure of the liquid oxygen tank meets the set value or not through the pressure measured by the pressure sensor C, if yes, the execution of the automatic pressurization program is finished, and the automatic pressurization is finished through a function button for stopping pressurization on an operation interface of automatic flow operation software of the constant pressure valve of the upper computer.
2. The protection method of the automatic flow control system based on liquid oxygen flow regulation as claimed in claim 1, wherein an operator can stop the automatic pressurization process at any time through a function button for pressurization stop on an operation interface of automatic flow operation software of the constant pressure valve.
3. The protection method of the automatic flow control system based on liquid oxygen flow regulation as claimed in claim 1, wherein an operator intervenes in the pressurization process according to the pressurization condition of the liquid oxygen tank, i.e. during the pressurization process, the valve can be operated by the PLC, the automatic pressurization program is stopped, and the state of the non-operated valve is maintained, i.e. the constant pressure valve is normally open and the pressurization stop valve is normally closed.
4. The protection method for the automatic process control system based on liquid oxygen flow regulation as claimed in claim 1, wherein the pressure-increasing set value input box on the operation interface of the automatic process operation software of the constant pressure valve of the upper computer is manually set, that is, the pressure set value of the constant pressure valve is manually input after every set time length A until the pressure set value is equal to the pressure-increasing target value.
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CN203882159U (en) * 2014-06-20 2014-10-15 湖北理工学院 Intelligent control system based on regulating valve
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CN206348649U (en) * 2016-09-13 2017-07-21 北京理工大学 A kind of pneumoelectric Automated condtrol platform
CN109340571A (en) * 2018-11-30 2019-02-15 醴陵旗滨电子玻璃有限公司 Nitrogen supply system and its control method
CN109737303B (en) * 2018-12-25 2020-11-20 北京动力机械研究所 Liquid oxygen system

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