CN203745052U - Container parallel connection and reversing valve type pVTt method gas flow device - Google Patents

Abstract

The utility model discloses a container parallel connection and reversing valve type pVTt method gas flow device. The container parallel connection and reversing valve type pVTt method gas flow device comprises a standard container, a buffer container, an intelligent collecting system, a front gathering pipe and a back gathering pipe. An inlet end valve, a valve for combined selection and an outlet end valve are arranged on the standard container, a testing pipe is arranged on the front gathering pipe, and a spraying nozzle clamping section is arranged between the front gathering pipe and the back gathering pipe; an air outlet of the back gathering pipe is respectively connected with one end of a connecting pipe and one end of a by-pass pipe, the other end of the connecting pipe is connected with the outlet end valve, and the other end of the by-pass pipe is communicated with an air inlet of the buffer container; the intelligent collecting system collects the pressure and the temperature in the standard container, at the position of a tested instrument installation opening and in the testing pipe, the front gathering pipe and the back gathering pipe before and after air inflation and the air inflation time. By means of the container parallel connection and reversing valve type pVTt method gas flow device, a critical flow flowmeter can be detected with a static method, various gas flowmeters can be detected with a dynamic method, and particularly high-accuracy standard meters can be detected.

Description

Container parallel connection and reversing valve type pVTt method gas flow device

technical field

The utility model relates to a gas flow detection device, in particular to a container parallel connection and reversing valve type pVTt method gas flow device.

Background technique

The pVTt method gas flow detection device is a widely used primary gas flow standard metering device and equipment. It has a high level of accuracy, and the measurement uncertainty U can reach 0.07% or higher. Venturi is usually used as a secondary standard. Primary standard devices and equipment for traceability of critical flow flowmeters such as nozzles and sonic nozzles.

At present, whether the test pressure is positive pressure or negative pressure, the pVTt method gas flow device requires that the ratio of the pressure in the standard container before and after inflation to the pressure at the instrument under test should not be greater than the critical pressure ratio γ _* , and the value of γ _* is related to the test medium , pressure, the structure of the critical flow gas flowmeter to be tested, etc., usually γ _* is between 0.528 and 0.85, which limits the application and promotion of the current pVTt method gas flow detection device. The pVTt method gas flow device still has the following problems: (1) There is only one standard container; (2) The volume of the standard container is small, and the maximum flow value is small; (3) The flow range that can be verified is not wide and is specified as a certain range (4) Each device has only one turndown ratio and flow range, which cannot be combined; (4) It can only be used to detect the measurement characteristics of critical flow meters, and cannot detect other flow meters such as standard meters; (5) Due to the pVTt method When the gas flow device enters the air, the flow rate of the test pipeline changes with the pressure in the standard container, and the detection flow cannot be controlled or set; (6) The pVTt method gas flow device can only use the static method to detect the flow meter, that is, the flow meter at the beginning of the test The flow increases from zero to the set detection flow value, and the flow meter flow decreases from the set detection flow value to zero when it stops. When detecting flow meters other than the critical flow flow meter, the detection error will be large.

Utility model content

Aiming at the above-mentioned deficiencies in the prior art, the utility model provides a method that can realize not only the static detection of the critical flow meter, but also the dynamic detection of various gas flow meters, especially the parallel connection of containers with high-accuracy standard meters. Reversing valve type pVTt gas flow device.

In order to solve the above technical problems, the utility model adopts the following technical solutions:

Container parallel connection and reversing valve type pVTt method gas flow device, including standard container, buffer container, vacuum pump, intelligent collection system, front header and back header;

There are two or more standard containers, and each standard container is equipped with an inlet valve, a valve for combination selection and an outlet valve; the outlet of each inlet valve is connected to the corresponding standard container, and the outlet of each inlet valve The inlet is used as the installation port I of the instrument under test; one end of each combination selection valve is connected to the corresponding standard container, and the other end of each combination selection valve is connected to each other; one end of each outlet valve is connected to the corresponding standard container; A standard container communicates with the air inlet of the buffer container through valve I, and the buffer container is connected with the vacuum pump;

The header is provided with at least one test pipeline, and the test pipeline is sequentially provided with a valve K _m and an installation port II of the instrument under inspection from close to the header to far away from the header; There is at least one nozzle clamping section between the pipes, and the nozzle clamping section includes nozzles, transition pipes and valves K _j #; one end of the nozzle communicates with the header pipe, and the other end of the nozzle communicates with the transition pipe One end of the transition pipeline is connected to one end of the valve K _j #, and the other end of the valve K _j # communicates with the rear header;

The air outlet of the rear manifold is connected to one end of the connecting pipe and the bypass pipe respectively, and the other end of the connecting pipe is connected to the other end of each outlet valve; the other end of the bypass pipe is connected to the inlet of the buffer container. The air port is connected, and the valve K _F is installed on the bypass pipe;

The intelligent acquisition system includes pressure sensors and temperature sensors arranged on the standard container, at the installation port I of the instrument under test, on the test pipeline, on the front header and on the rear header, and the pressure sensor and temperature sensor on the test pipeline The sensor is set on the air intake front side of the installation port II of the instrument under test.

As a preferred solution of the present invention, a valve II is installed on the pipeline connecting the buffer container and the vacuum pump.

Compared with the prior art, the utility model has the following advantages:

1. Based on the principle of pVTt measurement, based on the design of the existing pVTt method gas flow detection device: (1) Multiple standard containers are used alone or combined arbitrarily to form different standard containers V, to achieve 1~(2 ⁿ -1)( n is the number of containers) the combination of measuring ranges; (2) increase the sonic nozzle group for pressure field isolation and flow setting; (3) increase the reversing valve, bypass pipe and control system; (4) increase the test pipeline, Detect flow meters of different calibers. Develop a set of volume combination and reversing valve type pVTt method gas flow device, which can not only detect the critical flow flowmeter by static method, but also can detect various gas flowmeters by dynamic method, especially the standard meter with high accuracy.

2. This device is based on the pVTt method and the dynamic detection principle of "reversing valve". The standard container in the device is composed of n containers, and the sonic nozzle assembly is used for pressure field isolation and flow adjustment and setting, so that the device can be used as a 2 ⁿ - A set of pVTt method gas flow detection device can also be used as a sonic nozzle gas flow detection device, that is, a set of devices has the technical characteristics of a 2 ⁿ device. During the detection process, the "reversing valve" is used to control the gas flow to realize the pVTt method. The device can dynamically detect the gas flow meter, especially the standard flow meter. In the measurement of this device: the measurement uncertainty of the pVTt method device can reach U=0.065%, k =2, and it can detect critical flow flowmeters (including sonic nozzles) and other gas flow meters of level 0.2 and below; sonic nozzles The measurement uncertainty of the gas flow detection device can reach U=0.25%, k =2, and can detect various gas flow instruments of grade 1 and below.

3. This flow device is equivalent to 2 ⁿ -1 sets of pVTt method, and it can also be used alone as a set of sonic nozzle parallel gas flow device with corresponding flow range. It occupies less area, lower cost, and the flow range can be combined. The test flow rate can be adjusted and set, and various gas flow meters can be detected, which will help the popularization and application of pVTt method devices.

Description of drawings

Figure 1 is a schematic diagram of the gas flow device (negative pressure) of the parallel connection of containers and the reversing valve type pVTt method;

Figure 2 is a schematic diagram of a 20m ³ pVTt method gas flow device (negative pressure) with parallel connection of containers and a reversing valve.

In the figure: 1—Inspected instrument (such as nozzle); 2—Standard container (built-in m temperature sensor); 3—Valve I; 4—Vacuum pump; 5—Valve II; 6—Buffer container; 7—Intelligent collection system; 8—control system; 9—connecting pipe; 10—bypass pipe; 11—rear header; 12—transition pipe; 13—flow setting nozzle; 14—front header; 15—rear straight pipe section; 16—inspected Instrument (standard meter); 17—test pipeline.

In Figure 2: the volume of the standard container 2 is V ₁ =10 m ³ (built-in 30 temperature sensors), V ₂ =20 m ³ (built-in 50 temperature sensors) two specifications; the test pipeline 17 adopts Ф200～Ф300 , Ф80～Ф150, Ф15～Ф65 three combination specifications.

Detailed ways

The utility model is described in further detail below in conjunction with the accompanying drawings and specific embodiments.

Figure 1 is a schematic diagram of a gas flow device (negative pressure) for parallel connection of containers and a reversing valve type pVTt method, including standard containers, buffer containers, vacuum pumps, intelligent collection systems, front headers and rear headers.

There are two or more standard containers, and each standard container is provided with an inlet valve, a combination selection valve and an outlet valve. The outlet of each inlet valve is connected to the corresponding standard container, and the inlet of each inlet valve is used as the installation port I of the instrument under test. One end of each combination selection valve communicates with the corresponding standard container, and the other end of each combination selection valve communicates with each other. One end of each outlet valve is connected to the corresponding standard container, and each standard container is connected to the air inlet of the buffer container through the valve I, the buffer container is connected to the vacuum pump, and the valve II is installed on the pipeline connecting the buffer container and the vacuum pump.

At least one test pipeline is provided on the header, and the valve K _m and the installation port II of the instrument to be tested are arranged in sequence on the test pipeline from close to the header to far away from the header. At least one nozzle clamping section is provided between the front header and the rear header, and the nozzle clamping section includes nozzles, transition pipes and valves K _j #. One end of the nozzle is connected to the front header, the other end of the nozzle is connected to one end of the transition pipe, the other end of the transition pipe is connected to one end of the valve K _j #, and the other end of the valve K _j # is connected to the rear header. The air outlet of the rear manifold is connected to one end of the connecting pipe and the bypass pipe respectively, and the other end of the connecting pipe is connected to the other end of each outlet valve; the other end of the bypass pipe is connected to the air inlet of the buffer container, and the bypass pipe Install the valve K _F on the pipe.

The intelligent acquisition system includes pressure sensors and temperature sensors set on the standard container, the installation port I of the instrument under test, the test pipeline, the front header and the rear header, and the pressure sensors and temperature sensors on the test pipeline are set at the The air intake front side of the installation port II of the inspection instrument; the intelligent acquisition system is used to collect in real time the pressure p and temperature T in the standard container before and after inflation, at the installation port I of the instrument to be inspected, and in the test pipeline, front header and rear header, as well as the inflation Time t, humidity, etc. are calculated and processed to obtain the detection results. The control system is used to control the valves at the inlet end, valves for combined selection, valves at the outlet end, valve I, valve II, valve K _F , valve K _m and valve K _j #, start and stop of the vacuum pump and selection of nozzles.

Explanation for Figure 1:

1. The standard volume V consists of n standard volumes from V ₁ to V _n , and there are 2 ⁿ -1 combinations in total to form a standard container group with a maximum volume of V=(V ₁ + V ₂ +...V _n ), and control K _1,1 /K _1,2 ～K _n,1 /K _n,2 realize the independent use and combined use of standard containers. The sonic nozzle is used for pressure field isolation, flow control and setting, K _1,2 ~ K _{n, 2} and bypass valve K _F form a reversing valve group, and various caliber test pipes are added to test flowmeters of various calibers and models. The control system automatically controls the intake pipe valve and bypass pipe valve to realize the function of "n-position one-way reversing valve", and uses the working principle of "reversing valve" to realize dynamic detection of flow meters in pVTt method gas flow devices, especially high-accuracy ones. standard table.

2. K ₁ ~K _m selects valves for the flowmeter to be tested. K _1,0 ～K _n,0 are open, K _1,1 ～K _n,1 and K _1,2 ～K _n,2 are closed, to realize the detection of critical flow flowmeter (such as nozzle) by static detection method. K _1,1 ～K _n,1 and K _1,2 ～K _n,2 open, K _1,0 ～K _n,0 close, use the nozzle as pressure field isolation, flow control and setting, adopt static or dynamic detection Ways to detect various types of flowmeters to be tested.

3. Z ₁ ~ Z _j are sonic nozzles with different opening diameter d and flow rate, these nozzles isolate the pressure field in the standard container from the pressure field at the instrument under test; K ₁ # ~ K _j # are high vacuum valves, controlling these The opening and closing of the valve controls and sets the flow rate. The sonic nozzle is used as the isolator between the pressure field in the standard container and the pressure field at the instrument under test, so that the pressure at the instrument under test will not change suddenly due to pressure changes in the standard container, and protect the instrument under test from sudden changes in pressure and flow. destroy. Use the sonic nozzle group and the corresponding caliber valve group to control, adjust and set the flow rate upstream of the standard container. The volumetric flow rate of the sonic nozzle is 0.5 m ³ /h, 1 m ³ /h, 2 m ³ /h... 2 ^(m-1) m ³ /h (m is the number of nozzles), and the maximum flow rate is guaranteed to be The detection flow rate can be adjusted within the range of 2 ^{mm 3} /h, and the sensitivity of flow adjustment is the state flow rate of the smallest nozzle. Large manifolds are arranged before and after the sonic nozzle group to measure stagnation pressure and temperature when the nozzle is in use. Add corresponding test pipe sections at the front header according to the flow rate and the diameter of the testing instrument.

4. K _1,2 ~ K _n,2 , K _F form "n-position one-way reversing valve". When K _1,0 ～K _n,0 are normally closed: After the gas flows through the meter under test, the selected nozzle Z _i and the rear header, when K _1,2 ～K _n,2 are closed, the bypass valve K _F is opened, and the gas Enter the buffer container through the bypass pipe, and the gas in the buffer container is pumped away by the vacuum pump; according to the detected flow rate, combine V ₁ ~ V _n standard containers and control the corresponding K _1,2 ~ K _n,2 switch, and close the bypass valve K _F Inflate the selected standard container.

5. p, T, t are pressure, temperature and time measurements respectively; ↓, ↑, ← are gas flow directions.

6. The buffer vessel can be composed of one or more pressure vessels according to the flow rate of the device.

7. The control system is used to control valve switch, nozzle selection, start and stop of vacuum pump, etc.

8. The intelligent acquisition system is used for real-time acquisition of the pressure and temperature in the standard container before and after inflation, at the installation port of the instrument to be inspected, as well as the inflation time, humidity, etc., and calculate and process to obtain the detection results.

The device consists of a combined standard container group, "n-position one-way reversing valve", front and rear manifolds, nozzle assemblies and their switching pipes, flow meter detection pipes, working air source, collection system, control system, etc. The working air source can be generated by a vacuum pump, an air compressor, etc., or it can be connected to an external vacuum air source or high-pressure air source. According to the needs, design test pipes of different calibers and install them in front of the header. Each test pipe is composed of front and rear straight pipe sections, valves, pressure temperature and pressure measuring interfaces, etc., and the flow meter to be tested is installed between the front and rear straight pipe sections. Between the front header and the rear header, the number n of nozzles to be installed is determined according to the flow range of the device and the sensitivity of the flow setting, and n nozzle clamping sections are installed. Each nozzle clamping section is composed of nozzles, transition sections, valves, etc. Both the front header and the back header are equipped with pressure and temperature pressure interface, and the valve in the clamping section of the control nozzle can control and set the flow rate.

Figure 2 is a schematic diagram of a 20m ³ pVTt method gas flow device (negative pressure) with parallel connection of containers and a reversing valve. The device is composed of a 10m ³ standard container, a 20m ³ standard container, connecting pipes and valves, and can detect a maximum flow rate of 3000 m ³ /h class 0.2 critical flow meter (including sonic nozzle) and various other gas flow meters, especially standard meters.

The upstream of the standard container of the device uses the sonic nozzle group to stabilize and adjust the flow rate. The upstream and downstream of the nozzle group are designed with DN400 manifolds. Each nozzle is equipped with a high-vacuum baffle valve. The volume flow rate of the 14 sonic nozzles under standard conditions is respectively 0.5 m ³ /h, 1 m ³ /h, 2 m ³ /h...2048 m ³ /h, adjustable flow range (0.5-4096) m ³ /h.

A DN400 high-vacuum flapper valve is installed at the inlet of each container of the device, and a DN80 pipe is used to connect the two containers, and the connection is controlled by a high-vacuum flapper valve. The suction/release ports of the two containers are equipped with DN400 high vacuum baffle valves, which are connected to the main pipeline of the gas source of the vacuum pump. When using a 10m ³ standard container, use a 20m ³ standard container as a buffer container, and use K _1,2 and K _F to form a reversing valve group; when using a 20m ³ standard container, use a 10m ³ standard container as a buffer container and use K _2,2 And K _F form the reversing valve group. When using a 30m ³ standard container, turn on the vacuum pump, open the DN80 high vacuum damper valves K _1,1 and K _2,1 between the 10m ³ standard container and the 20m ³ standard container, and K _1,2 , K _2,2 and K _{and F} form the reversing valve group.

The device uses three 0.04-level Rosemount absolute pressure transmitters to measure the pressure in the ^10m3 container, the ^20m3 container, and the instrument respectively, and uses three 16-bit high-precision A/D modules to convert the voltage signal into a digital signal; Use 30 pt100 temperature sensors to measure the average temperature in a 10m ³ container, 50 pt100 temperature sensors to measure the average temperature in a 20m ³ container, and 1 pt100 temperature sensor to measure the temperature at the instrument, use 27 3-channel 8017 temperature modules to connect the resistance The value is converted into a temperature digital signal, and two 8520 communication modules are used to communicate the digital signal with the computer serial port and feed it back to the control program. The device uses the PCX8354 card as the control board to collect/control instrument pulse signals, valve start and stop signals, and time.

Finally, it is noted that the above embodiments are only used to illustrate the technical solutions of the present utility model without limitation. Although the utility model has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the utility model can be Modifications or equivalent replacements of the technical solutions without departing from the purpose and scope of the technical solutions of the utility model shall be covered by the claims of the utility model. the

Claims (2)

1. container parallel connection and reversal valve formula pVTt method gas flow meter, is characterized in that: comprise volumetric standard, buffer container, vacuum pump, intelligent acquisition system, front header and rear header;

Volumetric standard is two or more, is equipped with entrance point valve, combination selection valve and endpiece valve on each volumetric standard; The outlet of each entrance point valve and connection in corresponding volumetric standard, the import of each entrance point valve is as tested instrument installing port I; Each combination was selected with one end of valve and corresponding interior connection of volumetric standard, and each combination is selected to be interconnected with the other end of valve; One end of each endpiece valve and connection in corresponding volumetric standard; Each volumetric standard is communicated with the air intake opening of buffer container by valve I, and buffer container is connected with vacuum pump;

Described front header is provided with at least one test pipe, on described test pipe near header to setting gradually valve K away from front header _mwith tested instrument installing port II; Between described front header and rear header, be provided with at least one nozzle clamping section, described nozzle clamping section comprises nozzle, transition conduit and valve K _j#; One end of described nozzle is communicated with in front header, and the other end of described nozzle is connected with one end of transition conduit, the other end of described transition conduit and valve K _jone end of # connects, valve K _jthe other end of # is communicated with in rear header;

The gas outlet of described rear header is connected with one end of connecting pipe and by-pass pipe respectively, and the other end of described connecting pipe is connected with the other end of each endpiece valve; The other end of described by-pass pipe is communicated with the air intake opening of buffer container, mounted valve K on described by-pass pipe _f;

Described intelligent acquisition system comprise be arranged on volumetric standard, pressure transducer and temperature sensor in tested instrument installing port I place, test pipe, on front header and on rear header, the pressure transducer on described test pipe and temperature sensor are arranged on the air inlet front side of tested instrument installing port II.

2. container parallel connection according to claim 1 and reversal valve formula pVTt method gas flow meter, is characterized in that: mounted valve II on the pipeline that described buffer container is connected with vacuum pump.