CN205066891U - High accuracy pVTt method gas flow standard device - Google Patents

High accuracy pVTt method gas flow standard device Download PDF

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Publication number
CN205066891U
CN205066891U CN201520801858.8U CN201520801858U CN205066891U CN 205066891 U CN205066891 U CN 205066891U CN 201520801858 U CN201520801858 U CN 201520801858U CN 205066891 U CN205066891 U CN 205066891U
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China
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gas flow
method gas
water
standard device
temperature
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Expired - Fee Related
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CN201520801858.8U
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Chinese (zh)
Inventor
王振
邹海波
刘洋
巩晓龙
尚霜霜
郝松
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Liaoning Institute of Metrology
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Liaoning Institute of Metrology
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Abstract

High accuracy pVTt method gas flow standard device belongs to gas dosing test technical field, especially relates to a high accuracy pVTt method gas flow standard device's improvement. The utility model provides a high and the high high accuracy pVTt method gas flow standard device of precision of detection efficiency. High accuracy pVTt method gas flow standard device including volumetric standard, five tunnel switching control valve and control system, establishes digital pressure gauge and temperature sensor in the volumetric standard, the volumetric standard surface is equipped with vacuum tube way, digital pressure tap, temperature sensor interface, mudhole and measuring nozzle pipeline, its characterized in that: five tunnel switching control valves comprise two tee bend pneumatic valves, and two tee bend pneumatic valves all have an interface to feed through each other as connector, the connector of two tee bend pneumatic valves, and all the other four interfaces of five tunnel switching control valves are connected the vacuum tube way of vacuum pump, sound velocity nozzle, volumetric standard respectively and are detected the nozzle pipeline.

Description

High precision pVTt method gas flow standard device
Technical field
The utility model belongs to gas dosing technical field of measurement and test, especially relates to a kind of improvement of high precision pVTt method gas flow standard device.
Background technology
PVTt method gas flow standard device is the standard set-up of indirect inspection gas mass flow.Its principle is: device is in interval t sometime, and gas enters or discharge the volumetric standard that volume is V, according to the absolute pressure p of gas in volumetric standard before and after air inlet and the change of thermodynamic temperature T, calculates gas mass flow in testing process.Volumetric standard is first evacuated with vacuum pump before detecting by pVTt method gas flow standard device, this process is equivalent to volumetric standard and externally does work, in container, temperature reduces, and temperature imbalance (exhaust tube place temperature is lower) in container, now the temperature sensor inserted in volumetric standard can not truly reflect temperature in tank, vacuumize rear volumetric standard under normal circumstances and will stablize a few hours in isoperibol, the temperature after equalized temperature in volumetric standard in ability Measurement accuracy volumetric standard.In like manner, the stand-by period of a few hours is also needed after volumetric standard inflation.This greatly reduces the detection efficiency of pVTt method gas flow standard device.Pass through without flow in inflation front nozzle, when the valve between volumetric standard and nozzle is opened, nozzle front back pressure and rear back pressure is than change suddenly, and flow velocity is raised to suddenly local velocity of sound from zero, affects accuracy of detection.
Summary of the invention
The utility model is exactly for the problems referred to above, provides a kind of detection efficiency high and the high precision pVTt method gas flow standard device that precision is high.
For realizing above-mentioned purpose of the present utility model, the utility model adopts following technical scheme, high precision pVTt method gas flow standard device, comprise volumetric standard, five tunnel switching control valve and control system, digital pressure gauge and temperature sensor is established in volumetric standard, volumetric standard surface is provided with vacuum-pumping pipeline, digital pressure gauge interface, temperature sensor interface, mudhole and detection nozzle pipeline, it is characterized in that: described five tunnel switching control valve are made up of two threeway pneumatic valves, two threeway pneumatic valves all have an interface as connector, the connector of two threeway pneumatic valves is interconnected, all the other four interfaces of five tunnel switching control valve connect vacuum pump respectively, sonic nozzle, the vacuum-pumping pipeline of volumetric standard and detection nozzle pipeline.
As a kind of preferred version, in the middle part of the connector that two threeway pneumatic valves are connected, be provided with emptying pipeline.
As another kind of preferred version, described volumetric standard is made up of two connected column shape containers; In the middle part of two column shape containers and two ends connect and compose volumetric standard, increase the contact area of volumetric standard and water bath with thermostatic control, and being conducive to increases the heat transfer rate between volumetric standard and water bath with thermostatic control; Further, described volumetric standard volume is 110L, and the length of two column shape containers is 1600mm, diameter is DN200.
As another preferred version, above the threeway pneumatic valve be connected with sonic nozzle in five tunnel switching control valve, be provided with optoelectronic switch; When this threeway pneumatic valve action, the cylinder optoelectronic switch that moves up and down detects that namely cylinder moving sends signal to timer, and timer starts to record t detection time.
As another preferred version, be provided with pneumatic meter-clamping apparatus accordingly with sonic nozzle, described pneumatic meter-clamping apparatus is arranged at below sonic nozzle.Pore meter-clamping apparatus adopts inverted mounting means, is convenient to tong-test ammeter, and dust can be avoided to fall into, pollution norms container.
As another preferred version, described temperature sensor is accurate platinum sensor.
As another preferred version, described control system is take PLC as the control system of core, computer export port connects the programming port of PLC, the I/O output terminal of PLC controls the switch valve of the power supply of vacuum pump and two threeway pneumatic valves of five tunnel switching control valve, sonic nozzle arranges signal piping on front side of end, accurate platinum sensor is established in signal piping, accurate platinum sensor connects the input port of PLC by transmitter, two accurate platinum sensors that volumetric standard is arranged input computing machine by after analog signal figure by digital interface by digital watch, the pressure transducer that volumetric standard is arranged imports computing machine into through digital interface after converting pressure simulation signal to digital signal by digital pressure gauge, optoelectronic switch outputs signal to the I/O input end of timer and PLC, and timer-signals output terminal connects PLC input port.
As a kind of preferred version, described volumetric standard is placed in the water bath with thermostatic control of one-sided tomography overflow-type; Described one-sided tomography overflow-type water bath with thermostatic control, its apparatus main body includes water bath with thermostatic control cell body, refrigeration system, heating system, tank liquor circulation system, electric control system, it is characterized in that the constant temperature zone arranged in water bath with thermostatic control cell body is one-sided tomography overflow-type recycle design structure, wherein: the recirculated water of whole system, through refrigeration system, is injected into the buffer zone of constant temperature zone by feed pipe by tank liquor circulation system after heating system; Between the buffer zone and constant temperature zone of constant temperature zone, be placed with a porous water outlet orifice plate, the water in guarantee buffer zone enters constant temperature zone from bottom to top uniformly and carries out heat interchange with it; Be provided with a single-sided overflow formula manger board in one end of constant temperature zone, the part water covering this single-sided overflow formula manger board in water bath with thermostatic control flows into warm area to be controlled, then sucks temperature control module by ebullator, injects water bath with thermostatic control buffer zone, completes circulation.
Described feed pipe is one end water inlet, pvc pipe in the shutoff of one end, diameter 25mm, long 1800mm in water-bath, 100mm is provided with an apopore, because each hole exists pressure drop, equal in order to ensure each hole aquifer yield, described outlet water orifice diameter is processed into gradual change size, and the aquifer yield in each hole is 0.56L/min.Above-mentioned design ensure that thermostatted water enters the buffer zone of constant temperature zone uniformly.
Electric control system adopts PID regulable control, and temperature stability is good, and temperature-controlled precision is high.Continue by refrigeration machine the cold that relative constancy is provided, then by temperature controller, adopt PID to control heating system and carry out heating compensation, thus by constant for water temperature in the temperature range required.Porous water outlet orifice plate (bottom surface) top between water bath with thermostatic control and buffer zone arranges the platinum-resistance thermometer that a precision is ± 0.05 DEG C, by this platinum-resistance thermometer, measure the temperature of calibration cell water, temperature controller is according to the temperature of setting, solid-state relay is triggered, control the break-make of solid-state relay load end, thus regulate heating and cooling device add heat, reach the object of constant temperature.
Described one-sided tomography overflow-type recycle design refers to: arrange an one-sided tomography overflow baffle highly fixed in water bath with thermostatic control one end, recirculated water is by refrigeration heating system temperature control, water bath with thermostatic control buffer zone is injected by ebullator, constantly constant temperature zone is flowed into through too much emptying aperture plate, the water covering overflow baffle flows into warm area to be controlled, be recycled pump again and suck temperature-controlling system, complete circulation.
There is provided large scale, high uniformity by the water bath with thermostatic control of one-sided tomography overflow-type, the stable temperature field of low undulatory property, is placed in one the volumetric standard of pVTt device, and to ensure that in volumetric standard that gas vacuumizes the back balance time and is no more than 6min, detection efficiency is high.
The beneficial effects of the utility model.
The utility model volumetric standard, five tunnel switching control valve between nozzle and vacuum pump, are adopted to connect, first volumetric standard is evacuated during detection, then by five tunnel switching control valve, vacuum pump is connected with sonic nozzle, sonic nozzle is taken out with vacuum pump, then by five tunnel switching control valve, sonic nozzle is connected with volumetric standard, sonic nozzle flow is made to reach the flow of critical conditions before such calibrating, when ensure that in nozzle detection, valve events switches, the impact effectively avoiding the flow " sudden change " flowing through nozzle to bring, improves detection efficiency.Through China National Measuring Science Research Inst.'s calibrating, device expanded uncertainty is 0.05%(k=2), technical indicator reaches the highest level of domestic and international technical body same device.The detection of critical flow sonic nozzle can be carried out.
In addition, the water bath with thermostatic control of the utility model one-sided tomography overflow-type, adopts the recycle design of single-sided overflow from bottom to top, by fixed sturcture but not additional stirring system, reduces plant energy consumption.The design of gradual change porous oral siphon and multi-hole orifice, makes thermostatted water evenly flow into the whole region of water bath with thermostatic control, ensure that the temperature homogeneity that water bath with thermostatic control is good.Adopt and continue refrigeration electric heating PID adjustment control method, ensure that and the close-loop feedback that system temperature controls control bath temperature fast and accurately, ensure that the temperature fluctuation that water bath with thermostatic control is good.There is provided large scale, high uniformity by the water bath with thermostatic control of one-sided tomography overflow-type, the stable temperature field of low undulatory property, is placed in one the volumetric standard of pVTt device, and to ensure that in volumetric standard that gas vacuumizes the back balance time and is no more than 6min, detection efficiency is high.
Accompanying drawing explanation
Fig. 1 is the utility model volumetric standard schematic diagram.
Fig. 2 is the utility model five tunnel switching control valve structural representation.
Fig. 3 is the utility model volumetric standard and one-sided tomography overflow-type water bath with thermostatic control unitized construction schematic diagram.
Fig. 4 is the structural representation of one-sided tomography overflow-type water bath with thermostatic control.
Fig. 5 is the schematic diagram that one-sided tomography overflow-type water bath with thermostatic control controls basic circuit.
Fig. 6 is the structural representation of one-sided tomography overflow-type water bath with thermostatic control feed pipe.
Fig. 7 is the utility model one-piece construction schematic diagram.
In figure, 1 is vacuum-pumping pipeline, 2 is digital pressure gauge interface, 3 is temperature sensor interface, 4 is volumetric standard, 5 is mudhole, 6 for detecting nozzle pipeline, 7 is emptying pipeline, 8 is first interface, 9 is the second interface, 10 is the 3rd interface, 11 is the 4th interface, 12 is the water bath with thermostatic control of one-sided tomography overflow-type, 13 is liquid level, 14 is brace summer, 15 is water bath with thermostatic control cell body, 16 is warm area to be controlled, 17 is single-sided overflow formula manger board, 18 is porous water outlet orifice plate, 19 is feed pipe, 20 is platinum-resistance thermometer, 21 is temperature controller, 22 is solid-state relay, 23 is heating and cooling device, 24 is apopore, 25 is the second threeway pneumatic valve, 26 is the first threeway pneumatic valve, 27 is five tunnel switching control valve, 28 is sonic nozzle, 29 is signal piping, 30 is platinum-resistance thermometer, 31 is vacuum pump, 32 is optoelectronic switch.
Embodiment
A kind of high precision pVTt method gas flow standard device, comprise volumetric standard 4, five tunnel switching control valve 27 and control system, digital pressure gauge and temperature sensor is established in volumetric standard 4, volumetric standard surface is provided with vacuum-pumping pipeline 1, digital pressure gauge interface 2, temperature sensor interface 3, mudhole 5 and detects nozzle pipeline 6, digital pressure gauge interface 2 connects digital pressure gauge, temperature sensor interface 3 connects temperature sensor, and described temperature sensor is accurate platinum sensor; Described five tunnel switching control valve 27 are made up of two threeway pneumatic valves, two described threeway pneumatic valves are respectively the first threeway pneumatic valve 26 and the second threeway pneumatic valve 25, described first threeway pneumatic valve 26 and the second threeway pneumatic valve 25 all have a connector, are interconnected between two threeway pneumatic valves by described connector; Except described connector, the upper interface of described first threeway pneumatic valve 26 is first interface 8, lower interface is the second interface 9, the upper interface of the second threeway pneumatic valve 25 is the 3rd interface 10, lower interface is the 4th interface 11, is provided with emptying pipeline 7 between two interconnective connectors; The vacuum-pumping pipeline 1 of volumetric standard 4 connects the first interface 8 of five tunnel switching control valve 27, and the detection nozzle pipeline 6 of volumetric standard 4 connects the 3rd interface 10 of five tunnel switching control valve 27; Second interface 9 of five tunnel switching control valve 27 connects vacuum pump 31, and the 4th interface 11 that five tunnels switch pneumatic valve 27 connects sonic nozzle 28.
Described volumetric standard 4 is made up of two connected column shape containers; In the middle part of two column shape containers and two ends connect and compose volumetric standard, increase the contact area of volumetric standard and water bath with thermostatic control, and being conducive to increases the heat transfer rate between volumetric standard and water bath with thermostatic control; Further, described volumetric standard volume is 110L, and the length of two column shape containers is 1600mm, diameter is DN200.
Optoelectronic switch 32 is provided with above the threeway pneumatic valve be connected with sonic nozzle 28 in five tunnel switching control valve 27; When this threeway pneumatic valve action, the cylinder optoelectronic switch 32 that moves up and down detects that namely cylinder moving sends signal to timer, and timer starts to record t detection time.
Described control system is take PLC as the control system of core, computer export port connects the programming port of PLC, the I/O output terminal of PLC controls the switch valve of the power supply of vacuum pump 31 and two threeway pneumatic valves of five tunnel switching control valve 27, the accurate platinum-resistance thermometer arranged on front side of sonic nozzle 28 end connects the input port of PLC by transmitter, and two the accurate platinum sensors arranged in volumetric standard 4 input computing machine by after analog signal figure by digital interface by digital watch; The pressure transducer that volumetric standard is arranged imports computing machine into through digital interface after converting pressure simulation signal to digital signal by digital pressure gauge; Optoelectronic switch outputs signal to the I/O input end of timer and PLC, and timer-signals output terminal connects PLC input port.
In use procedure, first computing machine controls vacuum pump 31 and five tunnel switching control valve 27 by PLC, pressure in volumetric standard 4 is evacuated to setting value, by the accurate platinum resistance in volumetric standard 4 and digital pressure gauge measurement standard container inner pressure, feed back to computing machine, when pressure in volumetric standard arrives setting value, close vacuum-pump power supply, and close the connection between vacuum pump and volumetric standard by five tunnel switching control valve 27.Wait for equalized temperature, i.e. temperature difference between two platinum sensors in volumetric standard | start during T1-T2|≤0.1 DEG C to detect sonic nozzle.First in a computer t detection time is set, when starting to detect, five tunnel switching control valve states are vacuum pump, emptying pipeline, sonic nozzle be connected, " critical flow " is formed in sonic nozzle after opening vacuum pump, stablize 3 Miao Hou five tunnel switching control valve adaptive switched connected to the emptying pipeline of vacuum pump, sonic nozzle is connected with volumetric standard, and triggering optoelectronic switch, timer starts timing PLC and receives the feedback starting to detect.Self-closing control valve after timer periods arrives preset time t.Waiting for equalized temperature, i.e. two platinum sensor temperature differences in volumetric standard | temperature T1, T2 and pressure P in record standard container during T1-T2|≤0.1 DEG C, calculate the mass rate flowing through sonic nozzle in a computer.
Described volumetric standard 4 is placed in one-sided tomography overflow-type water bath with thermostatic control 12, is provided with brace summer 14 in one-sided tomography overflow-type water bath with thermostatic control 12, and described volumetric standard 4 is arranged on brace summer 14; Described one-sided tomography overflow-type water bath with thermostatic control 12, its apparatus main body includes water bath with thermostatic control cell body 15, refrigeration system, heating system, tank liquor circulation system, electric control system, it is characterized in that the constant temperature zone arranged in water bath with thermostatic control cell body 15 is one-sided tomography overflow-type recycle design structure, wherein: the recirculated water of whole system, through refrigeration system, is injected into the buffer zone of constant temperature zone by feed pipe by tank liquor circulation system after heating system; Between the buffer zone and constant temperature zone of constant temperature zone, be placed with a porous water outlet orifice plate 18, the water in guarantee buffer zone enters constant temperature zone from bottom to top uniformly and carries out heat interchange with it; Be provided with a single-sided overflow formula manger board in one end of constant temperature zone, the part water covering this single-sided overflow formula manger board in water bath with thermostatic control flows into warm area to be controlled, then sucks temperature control module by ebullator, injects water bath with thermostatic control buffer zone, completes circulation.
Described feed pipe is one end water inlet, pvc pipe in the shutoff of one end, diameter 25mm, long 1800mm in water-bath, 100mm is provided with an apopore, because each hole exists pressure drop, equal in order to ensure each hole aquifer yield, described outlet water orifice diameter is processed into gradual change size, and the aquifer yield in each hole is 0.56L/min.Above-mentioned design ensure that thermostatted water enters the buffer zone of constant temperature zone uniformly.
Electric control system adopts PID regulable control, and temperature stability is good, and temperature-controlled precision is high.Continue by refrigeration machine the cold that relative constancy is provided, then by temperature controller, adopt PID to control heating system and carry out heating compensation, thus by constant for water temperature in the temperature range required.Porous water outlet orifice plate (bottom surface) top between water bath with thermostatic control and buffer zone arranges the platinum-resistance thermometer that a precision is ± 0.05 DEG C, by this platinum-resistance thermometer, measure the temperature of calibration cell water, temperature controller 7 is according to the temperature of setting, solid-state relay is triggered, control the break-make of solid-state relay load end, thus regulate heating and cooling device add heat, reach the object of constant temperature.
Described one-sided tomography overflow-type recycle design refers to: arrange an one-sided tomography overflow baffle highly fixed in water bath with thermostatic control one end, recirculated water is by refrigeration heating system temperature control, water bath with thermostatic control buffer zone is injected by ebullator, constantly constant temperature zone is flowed into through too much emptying aperture plate, the water covering overflow baffle flows into warm area to be controlled, be recycled pump again and suck temperature-controlling system, complete circulation.
There is provided large scale, high uniformity by the water bath with thermostatic control of one-sided tomography overflow-type, the stable temperature field of low undulatory property, is placed in one the volumetric standard of pVTt device, and to ensure that in volumetric standard that gas vacuumizes the back balance time and is no more than 6min, detection efficiency is high.

Claims (10)

1. high precision pVTt method gas flow standard device, comprise volumetric standard (4), five tunnel switching control valve (27) and control system, volumetric standard establishes digital pressure gauge and temperature sensor in (4), volumetric standard (4) surface is provided with vacuum-pumping pipeline (1), digital pressure gauge interface (2), temperature sensor interface (3), mudhole (5) and detection nozzle pipeline (6), it is characterized in that: described five tunnel switching control valve (27) are made up of two threeway pneumatic valves, two threeway pneumatic valves all have an interface as connector, the connector of two threeway pneumatic valves is interconnected, all the other four interfaces of five tunnel switching control valve (27) connect vacuum pump (31) respectively, sonic nozzle (28), the vacuum-pumping pipeline (1) of volumetric standard (4) and detection nozzle pipeline (6).
2. high precision pVTt method gas flow standard device according to claim 1, is characterized in that: in the middle part of the connector that two threeway pneumatic valves are connected, be provided with emptying pipeline (7).
3. high precision pVTt method gas flow standard device according to claim 1, is characterized in that: described volumetric standard (4) is made up of two connected column shape containers.
4. high precision pVTt method gas flow standard device according to claim 1, is characterized in that: be provided with optoelectronic switch (32) above the threeway pneumatic valve be connected with sonic nozzle (28) in five tunnel switching control valve (27).
5. high precision pVTt method gas flow standard device according to claim 1, is characterized in that: be provided with pneumatic meter-clamping apparatus accordingly with sonic nozzle (28).
6. high precision pVTt method gas flow standard device according to claim 1, is characterized in that: described temperature sensor is accurate platinum sensor.
7. high precision pVTt method gas flow standard device according to claim 1, it is characterized in that: described control system is take PLC as the control system of core, computer export port connects the programming port of PLC, the I/O output terminal of PLC controls the switch valve of the power supply of vacuum pump and two threeway pneumatic valves of five tunnel switching control valve, sonic nozzle arranges signal piping on front side of end, accurate platinum sensor is established in signal piping, accurate platinum sensor connects the input port of PLC by transmitter, two accurate platinum sensors that volumetric standard is arranged input computing machine by after analog signal figure by digital interface by digital watch, the pressure transducer that volumetric standard is arranged imports computing machine into through digital interface after converting pressure simulation signal to digital signal by digital pressure gauge, optoelectronic switch outputs signal to the I/O input end of timer and PLC, and timer-signals output terminal connects PLC input port.
8. high precision pVTt method gas flow standard device according to claim 1, is characterized in that: described volumetric standard (4) is placed in one-sided tomography overflow-type water bath with thermostatic control (12); Described one-sided tomography overflow-type water bath with thermostatic control (12), its apparatus main body includes water bath with thermostatic control cell body (15), refrigeration system, heating system, tank liquor circulation system, electric control system, it is characterized in that the constant temperature zone arranged in water bath with thermostatic control cell body is one-sided tomography overflow-type recycle design structure, wherein: the recirculated water of whole system, through refrigeration system, is injected into the buffer zone of constant temperature zone by feed pipe by tank liquor circulation system after heating system; Between the buffer zone and constant temperature zone of constant temperature zone, be placed with a porous water outlet orifice plate (18), the water in guarantee buffer zone enters constant temperature zone from bottom to top uniformly and carries out heat interchange with it; Be provided with a single-sided overflow formula manger board in one end of constant temperature zone, the part water covering this single-sided overflow formula manger board in water bath with thermostatic control flows into warm area to be controlled, then sucks temperature control module by ebullator, injects water bath with thermostatic control buffer zone, completes circulation.
9. high precision pVTt method gas flow standard device according to claim 8, it is characterized in that: described feed pipe (19) is one end water inlet, pvc pipe in the shutoff of one end, diameter 25mm, long 1800mm in water-bath, be provided with an apopore at interval of 100mm, because each hole exists pressure drop, equal in order to ensure each hole aquifer yield, described outlet water orifice diameter is processed into gradual change size, and the aquifer yield in each hole is 0.56L/min.
10. high precision pVTt method gas flow standard device according to claim 8, is characterized in that: electric control system adopts PID regulable control; Continue by refrigeration machine the cold that relative constancy is provided, then by temperature controller, adopt PID to control heating system and carry out heating compensation, thus by constant for water temperature in the temperature range required; Above porous water outlet orifice plate between water bath with thermostatic control and buffer zone, the platinum-resistance thermometer that a precision is ± 0.05 DEG C is set, by this platinum-resistance thermometer, measure the temperature of calibration cell water, temperature controller is according to the temperature of setting, solid-state relay is triggered, control the break-make of solid-state relay load end, thus regulate heating and cooling device add heat.
CN201520801858.8U 2015-10-13 2015-10-13 High accuracy pVTt method gas flow standard device Expired - Fee Related CN205066891U (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105526996A (en) * 2015-10-13 2016-04-27 辽宁省计量科学研究院 A high-precision pVTt method gas flow standard device
CN105928592A (en) * 2016-04-27 2016-09-07 中国计量大学 Rapid detection pVTt methodgas flow standard device and detection method
CN109211369A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of pVTt method gas flow standard detection system
CN109211366A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of Multipurpose gas flow standard device based on air supply system
CN109211368A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of pVTt method gas flow standard system with control equipment
CN109211364A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of Multipurpose gas flow standard system with control equipment
CN109211365A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of multipurpose pVTt method gas flow standard device
CN109211367A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of pVTt method gas flow standard device
CN109211370A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of multipurpose pVTt method gas flow standard detection system
CN109211371A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of pVTt method gas flow standard device based on air supply system

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105526996A (en) * 2015-10-13 2016-04-27 辽宁省计量科学研究院 A high-precision pVTt method gas flow standard device
CN105526996B (en) * 2015-10-13 2018-10-12 辽宁省计量科学研究院 High-precision pVTt method gas flow standard devices
CN105928592A (en) * 2016-04-27 2016-09-07 中国计量大学 Rapid detection pVTt methodgas flow standard device and detection method
CN109211369A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of pVTt method gas flow standard detection system
CN109211366A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of Multipurpose gas flow standard device based on air supply system
CN109211368A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of pVTt method gas flow standard system with control equipment
CN109211364A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of Multipurpose gas flow standard system with control equipment
CN109211365A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of multipurpose pVTt method gas flow standard device
CN109211367A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of pVTt method gas flow standard device
CN109211370A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of multipurpose pVTt method gas flow standard detection system
CN109211371A (en) * 2018-09-28 2019-01-15 镇江市计量检定测试中心 A kind of pVTt method gas flow standard device based on air supply system

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