Gas and liquid property detection system
By designing a gas -liquid detection system that includes gas supply pipelines, liquid supply pipelines, and gas -liquid response devices, the problem of poor accuracy of gas liquid detection in existing technologies has been solved, and accurate determination and accuracy of gas -liquid response is achieved. Fast acquisition of properties.
Patent Information
- Application Number
- CN202211166261.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2022-09-23
- Publication Date
- 2025-01-28
- Estimated Expiration
- 2042-09-23
AI Technical Summary
The existing gas-liquid properties detection methods are greatly affected by environmental factors, resulting in poor accuracy of the measurement results.
A gas -liquid -based detection system is designed, including the gas supply pipeline, liquid supply pipeline and gas liquid response device. By setting up gas and liquid preheats on the gas pipeline and liquid supply pipeline, the temperature of the gas and liquid is ensured, and the dissolving and diffusion of the gas and liquid in the gas -liquid reaction device can be achieved, thereby improving the detection accuracy.
Through this system, the solubility and other properties of the gas -liquid reaction can be quickly and accurately determined, and the impact of temperature changes on the experimental results can be avoided, and the accuracy of the properties of gas liquid detection is significantly improved.
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Figure CN115508252B_ABST
Abstract
Description
Technical Field
[0001] The present application relates to the technical field of gas-liquid property detection, and in particular, to a gas-liquid property detection system. Background Art
[0002] The determination of gas-liquid reaction properties, such as the diffusion coefficient, solubility, reaction kinetics and other properties of gas-liquid, and the reliable design and development of gas-liquid reaction processes have important guiding significance in chemical operations and applications such as chemical engineering and environment.
[0003] In the related art, the determination of the solubility parameters of gas in liquid is usually carried out through the volume saturation method, pressure decay method, bubble point method and the like. However, the determination of gas-liquid properties is greatly affected by environmental factors (such as temperature), resulting in poor accuracy of the test results obtained by the existing experimental equipment and methods. Summary of the invention
[0004] The purpose of the embodiments of the present application is to provide a gas-liquid property detection system to improve the accuracy of gas-liquid property detection.
[0005] An embodiment of the present application provides a gas-liquid property detection system, comprising: a gas supply pipeline, one end of which is connected to a gas supply device, and a gas mass flow meter and a gas preheater are provided on the gas supply pipeline, and the gas preset device is used to adjust the temperature of the gas in the gas supply pipeline; a liquid supply pipeline, one end of which is connected to a liquid supply device, and a liquid preheater is provided on the liquid supply pipeline, and the liquid preset device is used to adjust the temperature of the liquid in the gas supply pipeline; a gas-liquid reaction device, the other ends of the gas supply pipeline and the liquid supply pipeline extend into the gas-liquid reaction device, and the gas in the gas supply pipeline can enter the liquid supply pipeline in the gas-liquid reaction device and dissolve in the liquid in the liquid supply pipeline; wherein the temperatures of the gas and liquid entering the gas-liquid reaction device are the same.
[0006] In the above implementation process, the gas-liquid property detection system includes: a gas supply pipeline, a liquid supply pipeline and a gas-liquid reaction device. Among them, one end of the gas supply pipeline is connected to the gas supply device, the gas supply device is used to provide a gas source, and a gas preheater is provided on the gas supply pipeline. The gas preheater can adjust the temperature of the gas in the gas supply pipeline and make the temperature of the gas reach a preset temperature threshold; one end of the liquid supply pipeline is connected to the liquid supply device, the liquid supply device is used to provide liquid for gas-liquid reaction, and a liquid preheater is provided on the liquid supply pipeline. The liquid preheater can adjust the temperature of the liquid in the liquid supply pipeline and make the temperature of the liquid in the liquid supply pipeline the same as the temperature of the gas in the gas supply pipeline. The other ends of the gas supply pipeline and the liquid supply pipeline extend into the gas-liquid reaction device. The gas-liquid reaction device can provide a closed gas-liquid reaction environment and can keep the temperatures of the gas and liquid consistent. In the gas-liquid reaction device, the gas can enter the liquid reaction tube through the tube wall of the liquid reaction tube and dissolve in the liquid in the liquid reaction tube. Therefore, after the system is stable, the solubility of the gas-liquid reaction can be quickly obtained by reading the indication of the gas mass flow meter, and the data of various properties of the gas-liquid reaction, such as the diffusion system and reaction kinetics, can be obtained through model fitting, thereby avoiding the influence of temperature changes on the test results of the gas-liquid reaction experiment and effectively improving the accuracy of the gas-liquid reaction experimental data.
[0007] It is worth noting that the liquid pipeline used for circulating liquid in the gas-liquid reaction device is a fluorine-containing polymer thin-walled tube, the gas pipeline used for circulating gas is a stainless steel tube, and the liquid pipeline is located inside the gas pipeline. In this way, the gas can be dissolved in the liquid in the liquid pipeline through the pipe wall of the liquid pipeline, and it is ensured that the liquid in the liquid pipeline cannot flow out into the gas pipeline through the pipe wall.
[0008] In a possible implementation, it further includes: an automatic pressure reducing valve, which is arranged on the gas supply pipeline and located between the gas supply device and the gas preheater.
[0009] In the above implementation process, the automatic pressure reducing valve has the function of automatically adjusting the gas pressure in the gas supply pipeline, that is, it can automatically reduce the inlet pressure in the gas pipeline to the required outlet pressure, and rely on the energy of the gas itself to automatically keep the outlet pressure stable, thereby improving the stability of the gas flow in the gas supply pipeline.
[0010] In a possible implementation, it also includes: a first pressure sensor, which is provided on the gas supply pipeline and located between the automatic pressure reducing valve and the gas preheater, and is used to detect the pressure value of the gas flowing out of the automatic pressure reducing valve; a controller, which is electrically connected to the automatic pressure reducing valve and the first pressure sensor, and the controller is used to receive the pressure value and control the automatic pressure reducing valve to perform an action according to the pressure value so that the pressure value is adjusted to a preset pressure value.
[0011] In the above implementation process, by setting a first pressure sensor between the automatic pressure reducing valve and the gas preheater, the first pressure sensor can monitor the pressure of the gas in the gas supply pipeline in real time and transmit the pressure signal to the controller. The controller can adjust the pressure setting value of the automatic pressure reducing valve according to the pressure signal detected by the first pressure sensor, thereby realizing the regulation of the outlet pressure in the gas supply pipeline, so as to test the gas and liquid under different pressures, and improve the automation level of the gas-liquid property detection process.
[0012] In a possible implementation, a first one-way valve is provided between the gas mass flow meter and the gas preheater; and / or a filter is provided between the automatic pressure reducing valve and the gas supply device.
[0013] In the above implementation process, the first one-way valve is used to control the on-off of the gas output and prevent the gas from flowing back to the gas mass flow meter, thereby improving the safety of product use.
[0014] The gas inlet valve is used to control the on-off between the gas supply device and the gas supply pipeline. The filter plays a filtering role and is used to filter impurities in the gas source, which helps to improve the cleanliness of the gas and ensure the accuracy of gas-liquid reaction data detection.
[0015] In a possible implementation, a liquid delivery pump is provided between the liquid supply device and the liquid preheater, and a first one-way valve is provided between the liquid delivery pump and the liquid preheater.
[0016] In the above implementation process, by arranging a liquid delivery pump on the liquid supply pipeline between the liquid supply device and the liquid cooling preheater, the liquid delivery pump can automatically control the flow rate, pressure and pressure pulsation of the liquid in the liquid supply pipeline, so as to facilitate the delivery of liquids with different flow rates, flow rates and pressures through the liquid supply pipeline. Therefore, by changing the liquid flow rate, the gas flow meter readings at different liquid flow rates can be obtained, and then the diffusion coefficient of the gas in the liquid can be obtained through model fitting.
[0017] The first one-way valve is used to realize the circulation of liquid in the liquid supply pipeline after passing through the liquid delivery pump, and can ensure the continuity of liquid supply by the liquid delivery pump.
[0018] In a possible implementation, a second pressure sensor is provided on the liquid supply pipeline, and the controller is electrically connected to the second pressure sensor and the liquid delivery pump.
[0019] In the above implementation process, by setting a second pressure sensor on the liquid supply pipeline, the second pressure sensor can monitor the pressure of the liquid in the liquid supply pipeline in real time and transmit the liquid pressure signal to the controller. The controller can control the liquid delivery pump to adjust the pressure of the liquid supply pipeline according to the liquid pressure signal detected by the second pressure sensor, so as to facilitate the reaction of liquids and gases at different pressures, thereby obtaining test data of the reaction of liquids and gases at different pressures.
[0020] Exemplarily, a pressure relief valve electrically connected to the controller is also provided on the air supply pipeline and the liquid supply pipeline. When the pressure of the air supply pipeline or the liquid supply pipeline is greater than a preset pressure threshold, the controller can control the pressure relief valve to perform an action to ensure the safe use of the air supply pipeline and the liquid supply pipeline.
[0021] In one possible implementation, a cold / hot regulating device is disposed outside the gas-liquid reaction device.
[0022] In the above implementation process, a heat and cold regulating device is arranged outside the gas-liquid reaction device. The heat and cold regulating device (such as a water bath or a heating and cooling device, etc.) can regulate the temperature inside the gas-liquid reaction device so that the temperature inside the gas-liquid reaction device can be maintained at a preset temperature and kept constant, so as to measure the parameters of the gas-liquid reaction in the gas-liquid reaction device under different temperature conditions.
[0023] In a possible implementation, it further includes: a gas output pipeline and a liquid output pipeline, wherein the gas output pipeline and the liquid output pipeline are respectively connected to the gas outlet and the liquid outlet of the gas-liquid reaction device.
[0024] In the above implementation process, the gas output pipeline is connected to the gas outlet of the gas-liquid reaction device, and is used to supply the gas after the gas-liquid reaction is completed to discharge the gas-liquid reaction device; the liquid output pipeline is connected to the liquid outlet in the gas-liquid reaction device, and is used to supply the liquid after the gas-liquid reaction is completed to discharge the gas-liquid reaction device.
[0025] In a possible implementation, a third pressure sensor, a pneumatic ball valve and a first automatic back pressure valve are provided on the gas output pipeline.
[0026] In a possible implementation, a fourth pressure sensor and a second automatic back pressure valve are provided on the liquid output pipeline.
[0027] In the above implementation process, a third pressure sensor is arranged on the gas output pipeline, and a fourth pressure sensor is arranged on the liquid output pipeline. Both the third pressure sensor and the fourth pressure sensor are electrically connected to the controller. The controller can control the first automatic back pressure valve on the gas output pipeline to adjust and maintain the output pressure of the gas in the gas output pipeline according to the pressure value of the gas in the gas output pipeline detected by the third pressure sensor, and control the second automatic back pressure valve to adjust and maintain the output pressure of the liquid in the liquid output pipeline according to the pressure value of the liquid in the liquid output pipeline detected by the fourth pressure sensor, so as to switch the dynamic and static experimental states. BRIEF DESCRIPTION OF THE DRAWINGS
[0028] In order to more clearly illustrate the technical solutions of the embodiments of the present application, the drawings required for use in the embodiments of the present application will be briefly introduced below. It should be understood that the following drawings only show certain embodiments of the present application and therefore should not be regarded as limiting the scope. For ordinary technicians in this field, other related drawings can be obtained based on these drawings without paying creative work.
[0029] Figure 1 A schematic block diagram of the structure of a gas-liquid property detection system provided in an embodiment of the present application.
[0030] Icons: 100-gas-liquid property detection system; 10-liquid supply pipeline; 101-liquid supply device; 102-liquid delivery pump; 103-second one-way valve; 104-liquid preheater; 105-second pressure sensor; 20-gas supply pipeline; 201-gas supply device; 202-gas inlet valve; 203-filter; 204-automatic back pressure valve; 205-gas mass flow meter; 206-first one-way valve; 207-gas preheater; 30-gas-liquid reaction device; 40-liquid output pipeline; 401-second automatic back pressure valve; 402-fourth pressure sensor; 50-gas output pipeline; 501-first automatic back pressure valve; 502-pneumatic ball valve; 503-third pressure sensor. DETAILED DESCRIPTION
[0031] The technical solutions in the embodiments of the present application will be described below in conjunction with the drawings in the embodiments of the present application.
[0032] It should be noted that similar reference numerals and letters represent similar items in the following drawings, so once an item is defined in one drawing, it does not need to be further defined and explained in subsequent drawings. At the same time, in the description of this application, the terms "first", "second", etc. are only used to distinguish the description and cannot be understood as indicating or implying relative importance.
[0033] Please refer to Figure 1The embodiment of the present application provides a gas-liquid property detection system 100, including: a gas supply pipeline 20, one end of the gas supply pipeline 20 is connected to a gas supply device 201, and a gas preheater 207 is provided on the gas supply pipeline 20, and the gas preset device is used to adjust the temperature of the gas in the gas supply pipeline 20; a liquid supply pipeline 10, one end of the liquid supply pipeline 10 is connected to a liquid supply device 101, and a liquid preheater 104 is provided on the liquid supply pipeline 10, and the liquid preset device is used to adjust the temperature of the liquid in the gas supply pipeline 20; a gas-liquid reaction device 30, the other ends of the gas supply pipeline 20 and the liquid supply pipeline 10 extend into the gas-liquid reaction device 30, and the gas in the gas supply pipeline 20 can enter the liquid supply pipeline 10 in the gas-liquid reaction device 30 and dissolve in the liquid in the liquid supply pipeline 10; wherein the temperatures of the gas and liquid entering the gas-liquid reaction device 30 are the same.
[0034] In the above implementation process, the gas-liquid property detection system 100 includes: a gas supply pipeline 20, a liquid supply pipeline 10 and a gas-liquid reaction device 30. Among them, one end of the gas supply pipeline 20 is connected to the gas supply device 201, the gas supply device 201 is used to provide a gas source, and the gas supply pipeline 20 is provided with a gas mass flow meter 205 and a gas preheater 207, the gas preheater 207 can adjust the temperature of the gas in the gas supply pipeline 20, and make the temperature of the gas reach a preset temperature threshold; one end of the liquid supply pipeline 10 is connected to the liquid supply device 101, the liquid supply device 101 is used to provide liquid for gas-liquid reaction, and the liquid supply pipeline 10 is provided with a liquid preheater 104, the liquid preheater 104 can adjust the temperature of the liquid in the liquid supply pipeline 10, and make the temperature of the liquid in the liquid supply pipeline 10 reach the preset temperature threshold; The temperature of the gas inside is the same, and the other ends of the gas supply pipeline 20 and the liquid supply pipeline 10 extend into the gas-liquid reaction device 30. The gas-liquid reaction device 30 can provide a closed gas-liquid reaction environment and can keep the temperature of the gas and liquid consistent. The gas and liquid can be fully dissolved and diffused in the gas-liquid reaction device 30, so that after the system is stable, the solubility of the gas-liquid reaction can be quickly obtained by reading the indication of the gas mass flowmeter 205, and the data of various properties of the gas-liquid reaction, such as the diffusion system and reaction kinetics, can be obtained through model fitting, thereby avoiding the influence of temperature changes on the test results of the gas-liquid reaction experiment, and effectively improving the accuracy of the gas-liquid reaction experimental data.
[0035] It is worth noting that the liquid pipeline used for circulating liquid in the gas-liquid reaction device 30 is a fluorine-containing polymer thin-walled tube, the gas pipeline used for circulating gas is a stainless steel tube, and the liquid pipeline is located inside the gas pipeline. In this way, the gas can be dissolved in the liquid in the liquid pipeline through the pipe wall of the liquid pipeline, and it is ensured that the liquid in the liquid pipeline cannot flow out into the gas pipeline through the pipe wall.
[0036] Please refer to Figure 1In a possible implementation, it also includes: an automatic pressure reducing valve 204, which is arranged on the gas supply pipeline 20 and located between the gas supply device 201 and the gas preheater 207.
[0037] In the above implementation process, the automatic pressure reducing valve 204 has the function of automatically adjusting the gas pressure in the gas supply pipeline 20, that is, it can automatically reduce the inlet pressure in the gas pipeline to the required outlet pressure, and rely on the energy of the gas itself to automatically keep the outlet pressure stable, thereby improving the stability of the gas flow in the gas supply pipeline.
[0038] Please refer to Figure 1 In a possible implementation, it also includes: a first pressure sensor, which is arranged on the gas supply pipeline 20 and is located between the automatic pressure reducing valve 204 and the gas preheater 207, and is used to detect the pressure value of the gas flowing out of the automatic pressure reducing valve 204; a controller, which is electrically connected to the automatic pressure reducing valve 204 and the first pressure sensor, and the controller is used to receive the pressure value and control the automatic pressure reducing valve 204 to perform an action according to the pressure value so that the pressure value is adjusted to a preset pressure value.
[0039] In the above implementation process, by setting a first pressure sensor between the automatic pressure reducing valve 204 and the gas preheater 207, the first pressure sensor can monitor the pressure of the gas in the gas supply pipeline 20 in real time and transmit the pressure signal to the controller. The controller can adjust the pressure setting value of the automatic pressure reducing valve 204 according to the pressure signal detected by the first pressure sensor, thereby realizing the adjustment of the outlet pressure in the gas supply pipeline 20, so as to test the gas and liquid at different pressures.
[0040] It is worth mentioning that the technical solution of the present application can not only improve the accuracy of the measurement of various parameters of the gas-liquid reaction, but also through the automatic control coordination between the controller and each valve and sensor, it is possible to shorten the measurement time of the entire gas-liquid reaction parameters to within 0.5min to 60min, thereby effectively improving the measurement efficiency of various parameters of the gas-liquid reaction.
[0041] Please refer to Figure 1 In a possible implementation, a first one-way valve 206 is provided between the gas mass flow meter 205 and the gas preheater 207 .
[0042] In the above implementation process, the first one-way valve 206 is used to control the on-off of the gas output and prevent the gas from flowing back to the gas mass flow meter 205, thereby improving the safety of product use.
[0043] Please refer to Figure 1 In a possible implementation, a gas inlet valve 202 and a filter 203 are provided between the automatic pressure reducing valve 204 and the gas supply device 201 .
[0044] In the above implementation process, the gas inlet valve 202 is used to control the on-off between the gas supply device 201 and the gas supply pipeline 20, and the filter 203 plays a filtering role, which is used to filter impurities in the gas, helping to improve the cleanliness of the gas and ensure the accuracy of gas-liquid reaction data detection.
[0045] Please refer to Figure 1 In a possible implementation, a liquid delivery pump 102 is provided between the liquid supply device 101 and the liquid preheater 104 , and a second one-way valve 103 is provided between the liquid delivery pump 102 and the liquid preheater 104 .
[0046] In the above implementation process, by arranging a liquid delivery pump 102 (such as a constant flow pump, a syringe pump, etc.) on the liquid supply pipeline 10 between the liquid supply device 101 and the liquid cooling preheater, the liquid delivery pump 102 can automatically control the flow rate, pressure and pressure pulsation of the liquid in the liquid supply pipeline 10, so as to facilitate the delivery of liquids with different flow rates, flow rates and pressures through the liquid supply pipeline 10. Therefore, by changing the liquid flow rate, the gas flow meter readings at different liquid flow rates can be obtained, and then the diffusion coefficient of the gas in the liquid can be obtained through model fitting.
[0047] The second one-way valve 103 is used to realize the circulation of the liquid on the liquid supply pipeline 10 after passing through the liquid delivery pump 102 , and can ensure the continuity of the liquid supply of the liquid delivery pump 102 .
[0048] Please refer to Figure 1 In a possible implementation, a second pressure sensor 105 is provided on the liquid supply pipeline 10 , and the controller is electrically connected to the second pressure sensor 105 and the liquid delivery pump 102 .
[0049] In the above implementation process, by setting a second pressure sensor 105 on the liquid supply pipeline 10, the second pressure sensor 105 can monitor the pressure of the liquid in the liquid supply pipeline 10 in real time and transmit the liquid pressure signal to the controller. The controller can control the liquid delivery pump 102 to adjust the pressure of the liquid supply pipeline 10 according to the liquid pressure signal detected by the second pressure sensor 105, so as to facilitate the reaction of liquids and gases at different pressures, thereby obtaining test data of the reaction of liquids and gases at different pressures.
[0050] Exemplarily, a pressure relief valve electrically connected to the controller is also provided on the air supply pipeline 20 and the liquid supply pipeline 10. When the pressure of the air supply pipeline 20 or the liquid supply pipeline 10 is greater than a preset pressure threshold, the controller can control the pressure relief valve to perform an action to ensure the safe use of the air supply pipeline 20 and the liquid supply pipeline 10.
[0051] In a possible implementation, a cold / hot regulating device (not shown in the figure) is disposed outside the gas-liquid reaction device 30 .
[0052] In the above implementation process, a heat and cold regulating device is provided outside the gas-liquid reaction device 30. The heat and cold regulating device (such as a water bath or a heating and cooling device, etc.) can regulate the temperature inside the gas-liquid reaction device 30, so that the temperature inside the gas-liquid reaction device 30 can be maintained at a preset temperature and kept constant, so as to measure the parameters of the gas-liquid reaction in the gas-liquid reaction device 30 under different temperature conditions.
[0053] Please refer to Figure 1 In a possible implementation, it also includes: a gas output pipeline 50 and a liquid output pipeline 40, and the gas output pipeline 50 and the liquid output pipeline 40 are respectively connected to the gas outlet and the liquid outlet of the gas-liquid reaction device 30.
[0054] In the above implementation process, the gas output pipeline 50 is connected to the gas outlet of the gas-liquid reaction device 30, and is used to supply the gas after the gas-liquid reaction is completed to discharge the gas-liquid reaction device 30; the liquid output pipeline 40 is connected to the liquid outlet in the gas-liquid reaction device 30, and is used to supply the liquid after the gas-liquid reaction is completed to discharge the gas-liquid reaction device 30.
[0055] Please refer to Figure 1 In a possible implementation, a third pressure sensor 503, a pneumatic ball valve 502 and a first automatic back pressure valve 501 are provided on the gas output pipeline 50; a fourth pressure sensor 402 and a second automatic back pressure valve 401 are provided on the liquid output pipeline 40.
[0056] In the above implementation process, a third pressure sensor 503 is provided on the gas output pipeline 50, and a fourth pressure sensor 402 is provided on the liquid output pipeline 40. The third pressure sensor 503 and the fourth pressure sensor 402 are both electrically connected to the controller. The controller can control the first automatic back pressure valve 501 on the gas output pipeline 50 to adjust and maintain the output pressure of the gas in the gas output pipeline 50 according to the pressure value of the gas in the gas output pipeline 50 detected by the third pressure sensor 503, and control the second automatic back pressure valve 401 to adjust and maintain the output pressure of the liquid in the liquid output pipeline 40 according to the pressure value of the liquid in the liquid output pipeline 40 detected by the fourth pressure sensor 402, so as to switch the dynamic and static experimental states.
[0057] The above description is only an embodiment of the present application and is not intended to limit the scope of protection of the present application. For those skilled in the art, the present application may have various changes and variations. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present application should be included in the scope of protection of the present application. It should be noted that similar reference numerals and letters represent similar items in the following drawings, so once an item is defined in one drawing, it does not need to be further defined and explained in the subsequent drawings.
[0058] The above is only a specific implementation of the present application, but the protection scope of the present application is not limited thereto. Any technician familiar with the technical field can easily think of changes or substitutions within the technical scope disclosed in the present application, which should be included in the protection scope of the present application. Therefore, the protection scope of the present application should be based on the protection scope of the claims.
[0059] It should be noted that, in this article, relational terms such as first and second, etc. are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Moreover, the terms "include", "comprise" or any other variants thereof are intended to cover non-exclusive inclusion, so that a process, method, article or device including a series of elements includes not only those elements, but also other elements not explicitly listed, or also includes elements inherent to such process, method, article or device. In the absence of further restrictions, the elements defined by the sentence "comprise a ..." do not exclude the existence of other identical elements in the process, method, article or device including the elements.
Claims
1. A gas-liquid property detection system, characterized in that: include: A gas supply pipeline, one end of which is connected to a gas supply device, and a gas mass flow meter and a gas preheater are provided on the gas supply pipeline, and the gas preheater is used to adjust the temperature of the gas in the gas supply pipeline; A liquid supply pipeline, one end of which is connected to a liquid supply device, and a liquid preheater is provided on the liquid supply pipeline, and the liquid preheater is used to adjust the temperature of the liquid in the gas supply pipeline; A gas-liquid reaction device, wherein the other ends of the gas supply pipeline and the liquid supply pipeline extend into the gas-liquid reaction device, and the gas in the gas supply pipeline can enter the liquid supply pipeline in the gas-liquid reaction device and dissolve in the liquid in the liquid supply pipeline; Wherein, the temperature of the gas and liquid entering the gas-liquid reaction device is the same; A first one-way valve is provided between the gas mass flow meter and the gas preheater; and / or, A gas inlet valve and a filter are provided between the automatic pressure reducing valve and the gas supply device.
2. The gas-liquid property measurement system according to claim 1, characterized in that: Also includes: An automatic pressure reducing valve is arranged on the gas supply pipeline and is located between the gas supply device and the gas preheater.
3. The gas-liquid property measurement system according to claim 2, characterized in that: A first pressure sensor is provided on the gas supply pipeline, and the first pressure sensor is provided between the automatic pressure reducing valve and the gas preheater, and is used to detect the pressure value of the gas flowing out of the automatic pressure reducing valve; A controller is electrically connected to the automatic pressure reducing valve and the first pressure sensor, and is used to receive the pressure value and control the automatic pressure reducing valve to perform an action according to the pressure value so that the pressure value is adjusted to a preset pressure value.
4. The gas-liquid property detection system according to claim 3, characterized in that: A liquid delivery pump is provided between the liquid supply device and the liquid preheater, and a second one-way valve is provided between the liquid delivery pump and the liquid preheater.
5. The gas-liquid property detection system according to claim 4, characterized in that: The liquid supply pipeline is provided with a second pressure sensor, and the controller is electrically connected to the second pressure sensor and the liquid delivery pump.
6. The gas-liquid property detection system according to any one of claims 1 to 5, characterized in that: A cold and hot regulating device is arranged outside the gas-liquid reaction device.
7. The gas-liquid property detection system according to any one of claims 3 to 5, characterized in that: It also includes: a gas output pipeline and a liquid output pipeline, wherein the gas output pipeline and the liquid output pipeline are respectively connected to the gas outlet and the liquid outlet of the gas-liquid reaction device.
8. The gas-liquid property detection system according to claim 7, characterized in that: The gas output pipeline is provided with a third pressure sensor, a pneumatic ball valve and a first automatic back-pressure valve, and the third pressure sensor and the first automatic back-pressure valve are electrically connected to the controller.
9. The gas-liquid property detection system according to claim 8, characterized in that: A fourth pressure sensor and a second automatic back-pressure valve are provided on the liquid output pipeline, and the fourth pressure sensor and the second automatic back-pressure valve are electrically connected to the controller.
Citation Information
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