CN109211365A - A kind of multipurpose pVTt method gas flow standard device - Google Patents
A kind of multipurpose pVTt method gas flow standard device Download PDFInfo
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- CN109211365A CN109211365A CN201811141389.6A CN201811141389A CN109211365A CN 109211365 A CN109211365 A CN 109211365A CN 201811141389 A CN201811141389 A CN 201811141389A CN 109211365 A CN109211365 A CN 109211365A
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- standard
- valve
- flow
- volumetric standard
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F25/00—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume
- G01F25/10—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume of flowmeters
- G01F25/15—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume of flowmeters specially adapted for gas meters
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F25/00—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume
- G01F25/10—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume of flowmeters
- G01F25/17—Testing or calibration of apparatus for measuring volume, volume flow or liquid level or for metering by volume of flowmeters using calibrated reservoirs
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Abstract
The invention discloses a kind of multipurpose pVTt method gas flow standard devices, including volumetric standard group comprising the volumetric standard of various criterion volume, the volumetric standard group divide into 0.1m3、3m3And 34m3The volumetric standard of normal volume specification, overall skid-mounted structure setting is all made of on verification table position, and configure the constant guarantee component pipeline system of temperature, for connecting each pipeline composition of the flow path between the volumetric standard group, the tong-test ammeter system and the air supply system, the volumetric standard group and the tong-test ammeter system of various criterion volume share a set of air supply system.Beneficial effects of the present invention: it is big with detection range, accuracy is high, have two kinds of detecting states of positive pressure and negative pressure, improve efficiency, and can be to velocity of sound mouth and the high-grade standard scale amount of progress biography.
Description
Technical field
Flow standard technical field of the present invention more particularly to a kind of multipurpose pVTt method gas flow standard dress
It sets.
Background technique
For the detection work for effectively carrying out Gas Energy Source instrument, the construction of China's gas flow standard device enters high speed
Period of expansion, but due to the otherness of manufacturing enterprise's technical level, cause standard set-up quality very different, while standard is sent
Inspection problem also becomes increasingly conspicuous.In conjunction with China's gas flow instrument magnitude tracing status and it can satisfy multiple industries to gas stream
Amount standard set-up effectively quickly carry out tracing to the source demand situation under, develop that range of flow is wide, accuracy is high, there is positive pressure and negative pressure
Two kinds of detection operating conditions, and can have very much to sonic nozzle and the pVTt method gas flow standard device of the high-grade standard scale amount of progress biography
It is necessary.
China possesses the unit of multipurpose pVTt method gas flow standard device its device in normal pressure and micro-positive pressure at present
Lower work, calibrating maximum flow only reach 1300m3/ h, has been unable to meet actual demand.And 0.2 grade of High-precision standard gas stream
Meter is widely used in during gas standard sets, but lacks science legal standard set-up offer is effectively traced to the source.
Summary of the invention
The purpose of this section is to summarize some aspects of the embodiment of the present invention and briefly introduce some preferable implementations
Example.It may do a little simplified or be omitted to avoid our department is made in this section and the description of the application and the title of the invention
Point, the purpose of abstract of description and denomination of invention it is fuzzy, and this simplification or omit and cannot be used for limiting the scope of the invention.
In view of above-mentioned existing problem, the present invention is proposed.
Therefore, it is an object of the present invention to provide a kind of multipurpose pVTt method gas flow standard device, accuracy is better than 0.1%
Positive pressure multipurpose pVTt method gas flow standard device, and can be achieved at the same time calibration sonic nozzle under positive pressure and normal pressure, with
And 0.2 grade of calibrating gas flowmeter can be demarcated.
In order to solve the above technical problems, the invention provides the following technical scheme: a kind of multipurpose pVTt method gas flow mark
Standard apparatus, including volumetric standard group comprising the volumetric standard of various criterion volume, the volumetric standard group divide into 0.1m3、
3m3And 34m3The volumetric standard of normal volume specification is all made of overall skid-mounted structure setting on verification table position, and configures
The constant guarantee component of temperature;Tong-test ammeter system is set on mobile microscope carrier and connect with each volumetric standard group, each
The tong-test ammeter system can carry out detection work independently or simultaneously;Air supply system is the volumetric standard group and the tong-test ammeter
System provides individual gas sources, further includes positive pressure gas source and negative pressure gas source, the operation for being respectively used to positive pressure and vacuumizing;Pipeline system
System, for connecting each pipeline composition of the flow path between the volumetric standard group, the tong-test ammeter system and the air supply system,
Described in positive pressure gas source and the negative pressure gas source share a set of pipe-line system;And the volumetric standard of various criterion volume
Group and the tong-test ammeter system share a set of air supply system.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: described
Verification table position is for placing 34m3Volumetric standard group platform position, corresponding carrying installation 34m3The volumetric standard group, and 34m3
The constant guarantee component of temperature of volumetric standard group configuration is set in constant temperature using water-jacket.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: described
Tong-test ammeter system further includes tested nozzle and standard scale, the mounting means of pipeline connection is used between the two and the pipe-line system, often
A pipeline is respectively provided with measuring instrumentss;According to the principle of mass conservation, through the mass flow of standard scale compared with the indicating value of checklist,
Complete the detection of checklist.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: described
Pipe-line system includes main line and manifold trunk branch;The main line is used for the tong-test ammeter system, volumetric standard group, air supply system
Triangular connection;The manifold trunk branch is several branch lines on the main line, by the air pressure of the air supply system
Flow path branch.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: described
When negative pressure gas source is the gas source of the volumetric standard group, device detection of negative pressure state comprising water ring vacuum pump and blade vacuum
Pump;When the positive pressure gas source is the gas source of the volumetric standard group, device is positive pressure detecting state, and the positive pressure gas source includes
Air compressor, cooler, drying machine and different pressures high pressure tank.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: also wrap
Include flow control system and control system;The flow control system and the volumetric standard group pass through the corresponding company of pipeline
It connects, and the flow control system includes the continuously adjustable critical flow generating apparatus of flow, using continuous control critical flow nozzle
The technology of flow;The control system uses two-stage separate test and control system, is capable of the carrying out automatically controlling of complete paired systems, data
Acquisition, data processing, report management and record printing.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: described
Flow control system further includes valve control assembly, under automatic Verification state, can be selected open by the control system
Close corresponding valve, and the switch of valve guaranteed in place by limit switch, and valve control mode be it is pneumatic, electronic or
It surges.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: described
Control system includes host computer, slave computer, data acquisition and actuator;The host computer can set temperature in human-computer interaction interface
Angle value, flow value, control device operation and stopping, and the host computer passes through Ethernet protocol and realizes between the slave computer
The reception of data is sent, and the probation redport to tested flowmeter can be generated according to institute's measured data;The slave computer includes that can compile
Range controller PLC, A/D module and D/A module, the A/D module is by temperature sensor, humidity sensor, pressure sensor, flow
The analog signal of meter output is converted into digital data transmission to programmable controller PLC, realizes the acquisition of data;The D/A module
Analog control signal output is converted by digital signal, realizes the control to the actuator.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: described
Data acquisition includes temperature sensor, humidity sensor, pressure sensor, proving flowmeter and tested flowmeter, above-mentioned output
Signal is analog signal;And the temperature sensor uses Pt100A grade platinum resistance, 0~50 DEG C, MPEV≤0.1 DEG C indexes
Value is not more than 0.01 DEG C;The pressure sensor uses 0.025 stage pressure transmitter;The humidity sensor uses temperature digital display
Meter, measurement range: 10%~99%RH, allowable error ± 2%RH.
A kind of preferred embodiment as multipurpose pVTt method gas flow standard device of the present invention, in which: described
Actuator is corresponding with the valve control assembly, further includes pneumatic control valve door, frequency converter, power controller and temperature and humidity
Adjuster;The signal that the frequency converter is exported by receiving PLC, controls the revolving speed of blower, the pneumatic control valve door passes through
It receives current analog signal and adjusts aperture, the two collective effect realizes the control to flow, the power controller and the temperature
Humidistat controls the gas temperature and environment temperature control room of outflow heat exchanger by receiving standard analog signal respectively
Interior temperature.
Beneficial effects of the present invention: the range of nozzle can be examined by expanding, big with detection range, accuracy is high, with positive pressure
It with two kinds of detecting states of negative pressure, improves efficiency, and velocity of sound mouth and the high-grade standard scale amount of progress biography can both be examined and determine (calibration)
Critical flow venturi nozzle standard can also examine and determine (calibration) high-precision gas flowmeter (such as gas roots flowmeter, Ke Liao
Sharp mass flowmenter, gas turbine meter etc.).
Detailed description of the invention
In order to illustrate the technical solution of the embodiments of the present invention more clearly, required use in being described below to embodiment
Attached drawing be briefly described, it should be apparent that, drawings in the following description are only some embodiments of the invention, for this
For the those of ordinary skill of field, without any creative labor, it can also be obtained according to these attached drawings other
Attached drawing.Wherein:
Fig. 1 is 34m shown in the first embodiment of the invention3The theory structure schematic diagram of volumetric standard;
Fig. 2 is 34m shown in the first embodiment of the invention3The air supply system theory structure schematic diagram of volumetric standard;
Fig. 3 is 34m shown in the first embodiment of the invention3The whole theory structure applied to air supply system of volumetric standard
Schematic diagram;
Fig. 4 is the enlarged diagram of A module in Fig. 3;
Fig. 5 is the enlarged diagram of B module in Fig. 3;
Fig. 6 is the enlarged diagram of C module in Fig. 3;
Fig. 7 is the enlarged diagram of D-module in Fig. 3;
Fig. 8 is 34m shown in second of embodiment of the invention3、3m3And 0.1m3It constitutes volumetric standard group and is applied to air supply system
Whole theory structure schematic diagram;
Fig. 9 is the enlarged diagram of E module in Fig. 8;
Figure 10 is the enlarged diagram of F module in Fig. 8;
Figure 11 is control system architecture schematic diagram in second of embodiment of the invention;
Figure 12 is the flowage structure schematic diagram that control system is realized in second of embodiment of the invention;
Figure 13 is the overall structure diagram of adjustable opening pneumatic operated valve described in the third embodiment of the invention;
Figure 14 is the overall structure diagram of the 4th kind of safty shield of the invention;
Figure 15 is the 4th kind of safty shield perspective view overall structure diagram of the invention;
Figure 16 is the visual angle overall structure diagram of the 4th kind of safty shield isometric bottom side of the invention;
Figure 17 is the 4th kind of safty shield schematic cross-sectional view of the invention.
Specific embodiment
In order to make the foregoing objectives, features and advantages of the present invention clearer and more comprehensible, right with reference to the accompanying drawings of the specification
A specific embodiment of the invention is described in detail, it is clear that and described embodiment is a part of the embodiments of the present invention, and
It is not all of embodiment.Based on the embodiments of the present invention, ordinary people in the field is without making creative work
Every other embodiment obtained, all should belong to the range of protection of the invention.
In the following description, numerous specific details are set forth in order to facilitate a full understanding of the present invention, but the present invention can be with
Implemented using other than the one described here other way, those skilled in the art can be without prejudice to intension of the present invention
In the case of do similar popularization, therefore the present invention is not limited by the specific embodiments disclosed below.
Secondly, " one embodiment " or " embodiment " referred to herein, which refers to, may be included at least one realization side of the invention
A particular feature, structure, or characteristic in formula." in one embodiment " that different places occur in the present specification not refers both to
The same embodiment, nor the individual or selective embodiment mutually exclusive with other embodiments.
Thirdly, combination schematic diagram of the present invention is described in detail, when describing the embodiments of the present invention, for purposes of illustration only,
Indicate that the sectional view of device architecture can disobey general proportion and make partial enlargement, and the schematic diagram is example, herein not
The scope of protection of the invention should be limited.In addition, the three-dimensional space of length, width and depth should be included in actual fabrication.
Simultaneously in the description of the present invention, it should be noted that the orientation of the instructions such as " upper and lower, inner and outer " in term
Or positional relationship is to be based on the orientation or positional relationship shown in the drawings, and is merely for convenience of description of the present invention and simplification of the description, and
It is not that the device of indication or suggestion meaning or element must have a particular orientation, be constructed and operated in a specific orientation, therefore
It is not considered as limiting the invention.In addition, term " first, second or third " is used for description purposes only, and cannot understand
For indication or suggestion relative importance.
In the present invention unless otherwise clearly defined and limited, term " installation is connected, connection " shall be understood in a broad sense, example
Such as: may be a fixed connection, be detachably connected or integral type connection;It equally can be mechanical connection, be electrically connected or be directly connected to,
Can also indirectly connected through an intermediary, the connection being also possible to inside two elements.For the ordinary skill people of this field
For member, the concrete meaning of above-mentioned term in the present invention can be understood with concrete condition.
Embodiment 1
A kind of multipurpose pVTt method gas flow standard device provided in the present embodiment, can be two kinds in positive pressure, negative pressure
It is used under operating condition, shares a set of pipeline, data acquisition, transmission, processing and control systems, detection work can be carried out independently or simultaneously
Make, and can be to high-precision gas flowmeter (such as 0.2 grade of gas roots flowmeter, coriolis mass flowmeters, gas-turbine
Flowmeter etc.) calibrating (calibration).The device includes volumetric standard group 100, tong-test ammeter system 200, flow control system, air supply system
300, control system and pipe-line system 400.Specifically, above-mentioned each component carries out open loop by pipe-line system 400 or closed loop connects
Connect, formed pipe path, wherein volumetric standard group 100 use existing overall skid-mounted structure, skid-mounted structure refer to by
Functional unit is integrated on a unsplit bedplate, can be with a kind of integration mode of integral installation, movement;So-called skid is by equipment
Movement, be just convenient to carry out using crowbar in place, verification table position and standard including installation corresponding with volumetric standard group 100
Container group 100 configures the constant guarantee component 101 of temperature, is set in constant temperature, is used using the water-jacket of the prior art in the present embodiment
It is controlled in the temperature of 100 surrounding of volumetric standard group.
As shown in Figures 1 to 3,34m involved in the present embodiment3Illustrate the gas flow standard for volumetric standard pVTt-101
The principle and process of device.Specifically, the device further includes being set to 34m in the present embodiment3The upstream volumetric standard pVTt-101
Tong-test ammeter system 200, by pipe-line system 400 respectively with 34m3The gas source that volumetric standard pVTt-101, tong-test ammeter system 200 connect
System 400, and the control system integrally controlled for device.Further, in referring to Fig.1,34m3Volumetric standard pVTt-
101 using overall skid-mounted structure settings on verification table position, and be configured with the constant guarantee component 101 of temperature, the constant guarantor of the temperature
Barrier component 101 uses existing water-jacket thermostat, follows including being set to the water above volumetric standard pVTt-101
Ring hopper, collet is in 34m3The water circulation stream and frequency converter SV-101, Yi Jiyong of volumetric standard pVTt-101 wall surface
Pump PU-101 in Water circulation hydrodynamics source.Tong-test ammeter system 200 is set on mobile pallet, which is to deposit in existing
Packaged type microscope carrier, tong-test ammeter system 200 includes checklist, telescoping tube TPS1 and adjustable flow spray in the present embodiment
Mouth FCN-101.Pipe-line system 400 includes main line 401 and manifold trunk branch 402, and main line 401 is for tong-test ammeter system 200, mark
Quasi- container group 100, the triangular connection of air supply system 300;Manifold trunk branch 402 is several branch lines on main line 401,
By the air pressure flow path branch of air supply system 300, for the pipeline pressure of each branch path, in order to preferably go to understand the present invention,
To be illustrated as in main line 401 with the part of gas source piping connection in figure first branch b1, second branch b2 and
Third branch a is disposed with muffler, starting pneumatic operated valve AV-101, telescoping tube TPS1, spray by the most upstream of first branch b1
Mouth, triple valve 3WV-101,34m3Volumetric standard pVTt-101, adjustable opening valve LDV-101 and pipe end pneumatic operated valve LCV-101,
And corresponding measuring device is set in the present embodiment, including be arranged between telescoping tube TPS1 and nozzle temperature sensor TT101,
Pressure sensor PT101 and temperature value display instrument TY101, pressure value display instrument PY101, are acquired by the sensor
The numerical value of corresponding detection is shown after measurement data in temperature value, pressure value display instrument.Wherein pressure sensor PT101 is existing
The sensor of some PTX5072 models;The present embodiment further includes for measuring 34m3Volumetric standard pVTt-101 temperature and pressure
Temperature sensor TT102, pressure sensor PT102 and be used for temperature controlled water circulation pipe SV101, and be located at herein
Temperature sensor TT102 is connect with data-interface EIU102A, and data-interface EIU102A can be connect with serial server, to adopting
The data of collection are shared and are analyzed;It further include temperature sensor TT601, the temperature value for measuring water circulation hopper temperature
Display instrument TY601.After the completion of the connection of above-mentioned positional relationship, first branch b1, second branch b2 are respectively and in air supply system
Negative pressure gas source 302 connects, and third branch a is located between starting pneumatic operated valve AV-101, telescoping tube TPS1, connects with positive pressure gas source 301
It connects.Working principle in the present embodiment: the switch of triple valve 3WV-101 and first branch b1 is opened first, with tong-test ammeter system 200
End is closed, by air supply system 300 to 34m3Volumetric standard pVTt-101 carries out level-one vacuum pumping, works as 34m3Volumetric standard
After temperature, pressure value display are stablized in pVTt-101, volumetric standard group 100 is carried out formally using air supply system 300 again
Operation is vacuumized, after postponing a period of time, system carries out judging whether to test to temperature, the pressure data of acquisition, works as mark
After temperature is stablized in quasi- container group 100, is carefully taken out by first branch b2, create the critical state of sonic nozzle.The process
In each valve be positive pressure gas source 301 connect operated pneumatic valve, be not excluded for the possibility using electrically-controlled valve or the valve that surges certainly.
It is air supply system theory structure schematic diagram provided in this embodiment referring to Fig. 2, specifically, the air supply system 300 wraps
Positive pressure gas source 301 and negative pressure gas source 302 are included, positive pressure gas source 301 can not only be as the gas source under positive pressure calibrating state, and is also
The offer of pneumatic operated valve involved in the present embodiment opens or closes power.First positive pressure gas source 301 include be set in basement according to
Air compressor, cooler, drying machine and the hand-operated valve MV501 of secondary connection;It is set to basement upper layer and hand-operated valve MV501
Sequentially connected 5m3High pressure air storing duct VT-601,36m3High pressure air storing duct VT-602,26m3High pressure air storing duct VT-603 and heat
Exchanger, the wet temp instrument HT600 for being set to heat exchanger end, and each high pressure air storing duct all configures temperature, pressure sensing
Device, it is identical as the detection instrument of above-mentioned standard container setting, manifold trunk is also set up on the pipeline of positive pressure gas source 301 in the present embodiment
HD, the manifold trunk HD paid by different pressures section pipeline, pneumatic operated valve are connect by pipeline with manifold trunk HD, realize pneumatic operated valve
It opens and closes, wherein the pipeline of positive pressure gas source 301 is located at 26m3The high pressure upstream end air storing duct VT-603 is arranged by there is flow tune
Save valve CV-101, CV-102, flow is adjusted by the aperture of regulating valve, and with flow control valve CV-101, CV-
102 and corresponding line temperature, pressure sensor connection controller PIC501, PIC502, for temperature in control piper and
Pressure parameter.Further, negative pressure gas source 302 includes that the liquid-ring type connecting with above-mentioned first branch b1, second branch b2 is taken out very
Sky pump VP-101, dry-type vacuum pumping are pumped VP-102, and are equally controlled using pneumatic operated valve, hand-operated valve between pipeline, on pipeline
Pressure sensor PT504 is set and carries out loine pressure detection.It vacuumizes operation and is divided into two-stage, use liquid-ring type vacuum pumping pump first
Progress slightly vacuumizes operation, then carries out second level using dry-type vacuum pumping pump and vacuumizes operation.After the completion, start to be tested
Preparation.
It is 34m in reference Fig. 33Volumetric standard platform position is applied to tong-test ammeter system 200, air supply system 300 and passes through pipeline
The whole theory structure schematic diagram that system 400 connects, 34m3It is shared under volumetric standard either positive pressure, negative pressure calibrating state a set of
Pipe-line system 400 and air supply system 300, and the switching power of pneumatic operated valve in pipeline is provided by positive pressure gas source 301, in order to become apparent from
Expression and convenient for those skilled in the art understand, be classified as tetra- parts A, B, C, D, and referring to shown in Fig. 4~6 be respectively
This tetrameric enlarged diagram.
Embodiment 2
In order to improve the efficiency of detection and adapt to the detection of different size in the present embodiment, in the present embodiment with first
In a embodiment the difference is that: further include verification table position specification be respectively specifically 0.1m3Volumetric standard platform position, 3m3Standard is held
Device platform position and 34m3Volumetric standard platform position;Respectively correspond 0.1m3、3m3And 34m3The standard of volumetric standard, different size is held
Device group 100 constitutes volumetric standard group, wherein 3m3、34m3Volumetric standard uses water-jacket thermostat, 0.1m3Volumetric standard is adopted
With water-bath type thermostat, three can simultaneously or independently carry out detection operation.Referring in Fig. 8~10, wherein Fig. 9,10 is in Fig. 8
E, the enlarged diagram of F module, wherein E is 3m3Volumetric standard, F 0.1m3Volumetric standard and 34m3Volumetric standard platform position is arranged side by side
Setting shares a set of tested instrument testing equipment.Specifically, volumetric standard group 100 is using existing different volumes specification
Volumetric standard, to meet in the short time stabilization of temperature and uniformly, wherein 34m3And 3m3Volumetric standard is designed using water-jacket,
And the sink and water circulation pipe of volume are computed for its mating setting, preferably, by 34m in the present embodiment3And 3m3Standard
The water leg of container is divided into six and four separate chambers according to calculated result respectively, and the water inlet line of each separate chamber is equal
The assembled unit for configuring vortex-shedding meter and valve, monitors and adjusts the flow of inlet water of each chamber in real time, utmostly improve
Water quantity of circulating water uniforms in collet, it is ensured that temperature collaborative in stabilization process in volumetric standard, and finally ensure that standard is held
The stable homogenization of temperature in device, for the water flow of each waters collet by being specifically designed, target is by gas in volumetric standard
The stabilization time of temperature controls the 0.1m within 90min3Volumetric standard is designed using water-bath type, is placed in specially designed water
In bath.
It further, further include being set to the tong-test ammeter system 200 of volumetric standard group upstream in the present embodiment, and each tong-test ammeter
System 200 is correspondingly connected with the volumetric standard of a specification, so that each tong-test ammeter system 200 can carry out detection independently or simultaneously
Work, and tong-test ammeter system 200 further includes tested nozzle and standard scale, and duct type installation side is used between the two and pipe-line system 400
Formula, and measuring instrumentss are respectively provided at each pipeline and the volumetric standard of each specification, middle measuring instrumentss include temperature in this implementation
Sensor, humidity sensor, pressure sensor, temperature sensor use Pt100A grade platinum resistance, 0~50 DEG C, MPEV≤0.1
DEG C, scale division value is not more than 0.01 DEG C;The pressure sensor uses 0.025 stage pressure transmitter;Humidity sensor uses digital display
Thermometer, measurement range: 10%~99%RH, allowable error ± 2%RH.Uncertainty is selected in pressure measurement in volumetric standard
For the transmitter of 0.01% (0~700) kPa abs, it is 0.04%, (- 30~700) that uncertainty is selected in pipeline pressure measurement
The transmitter of kPaG;The transmitter that atmospheric pressure measurement need to be 0.02%, (75~125) kPa abs with uncertainty.Similarly
The accuracy that temperature measures in each volumetric standard group 100 is most important, and existing middle benchmark container (is equivalent to the present embodiment acceptance of the bid
Quasi- container) clinical practice is uniformly distributed temperature measuring point, recommends to select OKAZAKI high-precision four-wire system platinum resistance, both ends respectively draw two
Conducting wire, wherein two are used as constant current input signal cable, to provide constant 1mA reference current, in addition two signal wires are used to
Its voltage value is measured, measurement circuit independently separates, and due to being isolated using input, output, power supply three, substantially reduces lead electricity
Resistance measures the error of resistance value to it, and accuracy is 0.05 DEG C, range is 0~50 DEG C, meanwhile, temperature probe diameter is less than
3.5mm can effectively reduce thermal resistance, the variation of the rapid reaction temperature of energy.
Due to answering multiple spot science to be distributed temperature measuring point, 34m in volumetric standard group 1003Volumetric standard, every cubic metre many
In 1 temperature measuring point, sum is no less than 40 temperature measuring points, 3m3When volumetric standard, temperature measuring point is no less than 8,0.1m3Volumetric standard,
Temperature measuring point is no less than 4, with reduce due in volumetric standard gas temperature it is uneven caused by uncertainty of measurement, standard
It is the transmitter of 0.01% (0~700) kPa abs, pipeline pressure measurement that uncertainty is selected in pressure measurement in container group 100
Selecting uncertainty is the transmitter of 0.04%, (- 30~700) kPaG;Atmospheric pressure measurement need to uncertainty be 0.02%,
The transmitter of (75~125) kPa abs.
Itd is proposed in the present embodiment the volumetric standard groups 100 of above-mentioned 3 different sizes by after pipe-line system connection side by side
A set of tested instrument test pipeline is shared under two kinds of operating conditions of positive pressure and negative pressure, is shared the shared sets of data of sets of data acquisition and is adopted
Collection, transmission, processing and control systems, have independent gas source, according to the principle of mass conservation, by standard set-up mass flow with
The indicating value of checklist compares, and completes the detection of checklist, can carry out detection work independently or simultaneously.It is answered in certain the present embodiment
When further including control system, and for the flow control system of piping flow control.Specifically flow control system is practical is
Each valve control assembly (i.e. pneumatic operated valve) in above-mentioned one embodiment, is correspondingly connected between each volumetric standard and pipeline,
And flow control system further includes the critical flow generating apparatus for having flow continuously adjustable, using continuous control critical flow nozzle flow
Technology.Valve control assembly can select switch respective valves under automatic Verification state, through control system, and pass through
Limit switch guarantees the switch of valve in place, and valve control mode is pneumatic, electronic or surges, it is clear that, the present embodiment
The control mode of middle pipeline valve is that the valve that Pneumatic opening & closing mode is connected with volumetric standard group 100 is gentle using pneumatically ending
The double valve combination of dynamic opening and closing ball valve, it is ensured that the gas zero leakage under high vacuum trystate and high-potting state,
The triple valve that is connected with volumetric standard group 100 is the principal element of package unit uncertainty level, and the device is using Japanese import
And patented product, triple valve commutating period meet Δ t≤1 × 10-4, reach requirement of ignoring;Design uses high-precision
The laser sensor of degree measures record to triple valve commutating period, according to the actual observation record of triple valve commutating period, threeway
Valve Theoretical Design commutating period error is less than 1ms.Pipeline control is realized with this.It is not difficult to find that should also certainly in the present embodiment
Including time measuring unit, the prior art is used, the timing of time measuring unit should be accurate and reliable, causes time measurement not true
Surely there are two types of the factors spent: first is that the stability of crystal oscillation frequency;Second is that A class uncertainty when timer, using existing
There is crystal oscillator sensor, resolving power is less than 0.1ms, and the stability of crystal oscillator 8h is better than 1 × 10-6, time measurement Composite Seismogram
For Urel=0.001% (k=2).Matched by the design of above each modular unit, the uncertainty calculation of device instantaneous flow is public
Formula is u1=(u2 v+u2 t+u2 p+u2 T+u2 Z+u2 Δt+u2 Δm)1/2, in formula: the relative standard uncertainty u of volumetric standard volumev=
0.025%;The relative standard uncertainty u of time measurementt=0.001%;The relative standard uncertainty u of pressure measurementp=
0.01%;The relative standard uncertainty u of temperature measurementT=0.017%;The relative standard uncertainty u of gas compressibility factorZ
=0.005%;And the time system difference relative standard uncertainty u of triple valveΔt=0.01%;The opposite mark of pressure measurement
Quasi- uncertainty uΔm=0.005%;The instantaneous flow relative uncertainty degree u of synthesis1=0.0335%, expanded uncertainty Urel
=0.067% (k=2).
The checklist range of flow that covering device design can examine and determine under negative pressure method is (0.2~1600) m3/ h, positive pressure method
Detectable range of flow is 0.5~400m down3/ h, positive pressure method pressure are 0.6MPa abs.1m3Or more volumetric standard phase
It is U to expanded uncertaintyrel=0.07% (k=2), 1m3The opposite expanded uncertainty of following volumetric standard is Urel=
0.1% (k=2);Room temperature control is at 15 DEG C~25 DEG C when device is run, temperature stability are as follows: ± 2 DEG C/for 24 hours, ± 0.5
℃/1h.The design of the covering device has fully considered the Proper Match of each section, stringent design, the configuration guaranteed mould of accuracy
Module unit, it is ensured that the uncertainty of package unit;Calibrating can be achieved in positive and negative platen press, and reserved suitable for the method for standard table in later period
Expansion interface and space, reach the standard for fully considering device and using, safety, and rational deployment, meet environmental protection drop
It makes an uproar the requirement improved efficiency.
Further, the realization of control system is illustrated, control system uses existing PIC or PLC in the present embodiment
Controller (programmable interrupt controller) corresponds to the PIC appended drawing reference in diagram.Further, according in existing control system
It should be noted that control system includes host computer, slave computer, data acquisition and actuator;Wherein host computer is to use
LabVIEW software programming controls the PC of program, can be in human-computer interaction interface set temperature value, flow value, control device operation
And stopping, and host computer can be given birth to by the reception, transmission of data between Ethernet protocol realization and slave computer according to institute's measured data
The probation redport of tested flowmeter in pairs;Slave computer includes programmable controller PLC, A/D module and D/A module, and A/D module will be warm
Degree sensor, humidity sensor, pressure sensor, flowmeter output analog signal be converted into digital data transmission to programmable
Controller PLC realizes the acquisition of data;Digital signal is converted analog control signal output by D/A module, realizes to actuator
Control.Data acquisition includes temperature sensor, humidity sensor, pressure sensor, proving flowmeter and tested flowmeter, defeated
Signal is analog signal out.Actuator part and above-mentioned valve control assembly adapt to comprising pneumatic control valve door, frequency converter,
Power controller and thermo hydrograph regulator, the signal that frequency converter is exported by receiving PLC, control the revolving speed of blower, pneumatic to adjust
It saves valve and adjusts aperture by receiving current analog signal, the two collective effect realizes the control to flow, power controller and temperature
Humidistat controls the gas temperature and environment temperature control room of outflow heat exchanger by receiving standard analog signal respectively
Interior temperature.
Referring to Fig.1 in 1, the present embodiment control system for example can be using the knot of centralized management, decentralised control, data sharing
Structure, Industrial Ethernet is for realizing the communication between management level and the controller of shop layer or between controller and PC, general number
According to measure larger, transmission range farther out, transmission rate it is fast, be suitable for bad environments and anti-interference demanding industry spot.This dress
It sets by using 3 existing temperature-detecting devices, respectively to 3 constant volume slots (volumetric standard of corresponding 3 different sizes
100) internal temperature is measured in real time group, and data are passed to host computer, and data sharing thus may be implemented.The present apparatus
3 pressure detecting instruments are additionally used, data acquisition are carried out to the pressure in 3 constant volume slots, to realize data sharing;And in heat
In exchanger and atmosphere, humidity measurement instrument and temperature and humidity pressure one detector real-time data collection are used respectively and is shared;Make simultaneously
With 3 T4CU, data collected are analyzed respectively, to judge whether test is completed.Firstly, will after the completion of test
Then these data transmissions provide every detail parameters of checklist, are finally uploaded to specified data into host computer
In library.This 3 T4CU operate 3 triple valves respectively, control entire experiment process, and total with 3 PC machine during the test
Enjoy data.Above all of data realize that the agreement used is RS-485 by one 16 mouthfuls of serial server.
Flow chart in 2 referring to Fig.1, together referring to Fig.1~10 in, the control principle based on PLC is accomplished by first order pumping
The process of vacuum is designed essentially according to the control sequence of PLC.When being vacuumized to constant volume slot (i.e. above-mentioned standard container group 100),
It is first separately turned on water-ring vacuum pump, BV105 and BV102, vacuum pump is made first to open operation;After postponing a period of time, close
BV102, then BV103, LDV101 and LCV101 are opened respectively, thus start that constant volume slot is carried out to vacuumize operation.In order to ensure
Pressure inside the tank is stablized, and after constant volume slot internal pressure reaches preset requirement, also needs to wait for a period of time.When pressure reaches centainly
After it is required that, LDC101, LCV101 and BV103 are closed, opens BV102, and wait the signal of above-mentioned valve in place;Finally, stopping
Only VP101 and BV102, the first order vacuumizes work and is basically completed at this time, needs to monitor constant volume slot internal pressure;If equipment is different
Often, then termination test is wanted;Test terminates must be according to certain process, to prevent equipment damage;It to be shown at this time in host computer simultaneously
Device is in test final state;The second level vacuumize vacuumized with the first order it is quite similar, difference be to use first
Dry-type vacuum pumping pump after dry vacuum pump startup, opens BV104 and take out very to constant volume slot so the pipeline used is different
Idle job.Before carrying out formal flowmeter detection test, it is also necessary to be prepared work, prepare process be it is extremely important,
It will directly affect the success or not of flowmeter detection test, mainly be carried out by user's selection using negative pressure method or positive pressure method
Test, as long as can make as long as host computer is selected slave computer PLC to device carry out practical operation.Further, work as use
When negative pressure method, AV101 is opened, pipeline is directly contacted with atmospheric pressure at this time;When selection is using positive pressure method, AV102 is opened, it is fixed to make
Product slot is connected with air accumulator, successively carries out flowmeter detection test.The present embodiment further includes designing monitoring system using LabVIEW
Picture, wherein including 3 pipeline pictures, the process for entirely testing.Meanwhile operator can directly operate from monitoring screen
Whole system also can learn that equipment is abnormal from monitoring system picture, in time make adjustment;It is necessary to when, can be tight
It is anxious to close whole equipment.
In Fig. 1~10, appended drawing reference involved in figure is as follows: (note: LCV-201 is equal with LCV201, other similarly)
Embodiment 3
In reference above-described embodiment, adjustable opening gas in multipurpose pVTt method gas flow standard device of the present invention
Valve is moved, is illustrated as CV101 or CV102 in figure, is used for the flow control of positive pressure pipeline, existing middle pneumatic control valve is with compressed gas
For power source, using cylinder as actuator, and by means of valve positioner, converter, solenoid valve, protect position valve, air accumulator, gas mistake
The attachmentes such as filter remove driving valve, can realize that switching value or proportion expression are adjusted, by way of adjusting aperture to adjust pipeline
Medium: the various parameters of technique process such as flow, pressure, temperature, liquid level.It should be noted that air rammer in the present embodiment
Executing agency uses compressed air source, i.e., passes through pipeline and pneumatic control valve using the gas source that air supply system 300 generates
Between be connected to, and by the movement of valve inner piston band ovable valve stem move up and down, reach the opening and closing for making valve.Art technology
Personnel are it should be understood that in real process, first is that pneumatic control valve installation site, requires have certain height away from ground,
Valve it is upper and lower will there are certain spaces, to carry out the dismounting and repairing of valve, for equipped with pneumatic positioner valve and handwheel
Regulating valve, must guarantee operation, observation and it is easy to adjust;Second is that regulating valve should be mounted on horizontal pipe, and hang down up and down with pipeline
Directly, it generally to be supported, be guaranteed solid and reliable under valve;And when installing, when bore and the process pipe of regulating valve be not identical
When, it should be connected using reduced pipe, in the installation of small-bore regulating valve, can be threadedly coupled, avoid bringing to regulating valve bigger
Additional stress, third is that by-pass line is arranged, it is therefore an objective to, can be right in the case where not stopping operation convenient for switching or manual operation
Regulating valve is overhauled.
Therefore the adjustable opening pneumatic operated valve that the present embodiment uses is as shown in figure 13, illustrates the present embodiment adjustable opening gas
The overall structure diagram of dynamic valve comprising valve 500, air rammer 600 and valve deck unit 700, the installation between three
Structure can refer in the prior art in such a way that screw thread is embedded in or is fixed using bolt.Specifically, valve 500 is a kind of pass
Closing member is the slide-valve of parallel gate plate, and closure member can be single disc or the double disc therebetween with spreading mechanism, flashboard
It to the pressing force of valve seat is controlled by acting on the pressure medium of floating flashboard or floating valve seat, if it is double disc Flat Sluice
Valve, then the spreading mechanism between two flashboards can supplement this pressing force, and flat gate valve can be divided into manual platform by driving method
Gate valve, Pneumatic flat-plate gate valve and driven plate gate valve.And the present embodiment is single valve plate, and drives valve by air rammer 600
Door 500 is turned on or off, and by this present embodiment using air pressure being the piston of power, therefore is able to use rubber material
Material because the opposite mode of surging will lead to rubber material using after a long time can aging, lead to sealing leak, there are certain
The problem of security risk.Air rammer 600 further includes cavity 601, the piston with sliding space in further the present embodiment
Ontology 602, valve rod 603 and indicating arm 604, piston only 602 are set in cavity 601 and are integral type solid construction, valve
603 upper end of bar is connect with piston only 602, and lower end is connected with the valve plate 501 being set in valve 500.It needs to illustrate
It is that piston only 602 can slide up and down in cavity 601, by injecting hydraulic or air pressure into 601 one end of cavity
Pressure in cavity 601 is caused to increase, so that it is mobile to the lesser one end of pressure to push piston only 602, otherwise similarly, and valve deck
Signal in such as figure of unit 700, the mode being fixed by bolts are installed on the both ends of valve 500.Further, in the present embodiment
In, valve 500 further includes pipeline 502, valve chamber 503 and valve seat 504;Valve chamber 503 is connected to 502 cross of pipeline, is understood that
, corresponding pipeline 502 is gas source pipe in multipurpose pVTt method gas flow standard device of the present invention, pneumatic operated valve
Door is used for the flow control of pipeline.Valve seat 504 is set in valve chamber 503, and valve plate 501 is set in valve seat 504 and by valve rod 603
It drives up and down, realizes the opening and closing of valve seat 504, valve deck unit 700 further includes 701 He of bonnet, for being arranged on lower end
Bottom flange 702;Mounting portion 701a is arranged in 701 upper end of bonnet, and mounting portion 701a is inserted into lower installing port by being threadedly engaged peace
Dress, and valve rod 603 passes through bonnet, 701 and connect with valve plate 501;Bottom flange 702 further includes the tail-hood connecting with 500 bottom end of valve
702a, the nesting hood 702b being set in the tail-hood 702a and foot piece 702c being set in tail-hood 702a and hood 702b.
It is 501 stress balance of valve plate in the case where valve chamber 503 has pressure that the purpose of foot piece 702c is arranged herein, it is ensured that is in valve
Standard-sized sheet or full off state avoid valve plate from receiving the pressure of medium and move up.
It should be noted that the mounting means up and down between piston only 602, valve rod 603 and indicating arm 604 can be adopted
With screw thread mounting means, prior art realization can refer to, while it is not difficult to visualize ability gets over personnel, valve rod 603 and indicating arm 604 are also
The telescopic rod with one can be merged into, that is, the telescopic rod merged entirely runs through the upper and lower ends of piston only 602, and both ends are stretched out
Part be valve rod 603 and indicating arm 604 in the present embodiment, and seal assembly is certainly existed in piston for sealing the gas
Piston equally can refer to prior art realization.Further, air rammer 600 further includes be set to lateral wall enterprising
Pressure mouth 605, under into pressure mouth 606 and be set to upper and lower end upper opening and lower installing port;Enterprising pressure mouth 605, under into pressure mouth
606 are separately connected pressure source, push piston only 602 to be located at by different pressure and move in cavity 601;Indicating arm 604
One end is connect with piston only 602, and the other end passes through in upper opening and realizes that sealing prevents from revealing by sealing block;Valve rod 603
One end is connect with piston only 602, and the other end is connect after passing through lower installing port with valve plate 501, similarly for valve rod 603 under
It is also that there is sealing structure identical with sealing block to be sealed in installing port.It should be noted that under mounting portion 701a insertion
By being threadedly engaged installation in installing port, screw thread mounting means is equally used, can refer to prior art realization and enterprising pressure mouth
605, it is connect into pressure mouth 606 with external pressure source under, and cavity 601 divides into epicoele and cavity of resorption, enterprising pressure by piston only 602
Mouthfuls 605 are connected to epicoeles, under into pressure mouth 606 be connected to cavity of resorption, when pressure is inconsistent in upper cavity pressure and cavity of resorption, piston can be driven
Ontology 602 is mobile to the lesser one end of pressure, therefore realizes the movement with ovable valve stem.
Embodiment 4
If the signal of Figure 14~17 is provided with upper opening 607 in the top of air rammer 600 referring in above-described embodiment,
And 604 one end of indicating arm is connect with piston only 602, the other end passes through upper opening 607 and slides up and down, and is made in piston
When industry, there can be a large amount of dust granule since upper opening 607 is exposed in air, in the air under adverse circumstances and fall
Into upper opening 607, so that the dust fallen in relative motion gap between indicating arm 604 and upper opening 607 both causes
Movement wear and increase, can have certain abrasion of particles lubricating oil is added, seriously affect the using effect of piston with
Service life.Therefore abrasion caused by dust is fallen by upper opening 607 in order to effectively reduce, the present embodiment is unlike the embodiments above
Place is: safty shield 800 is set above upper opening 607, the safty shield 800 is dust-proof for upper opening 607, and
Indicating arm 604 is exposed constantly to do stretching motion outside has certain security threat, therefore security protection to extraneous operator
Cover 800 also have for indicating arm 604 safety protection function, herein it should also be noted that, safty shield 800 with above open
Mounting means between mouth 607 realizes that those skilled in the art are it is not difficult to find that such as safty shield 800 using the prior art
Bottom setting opening inwardly and inner surface has the slot of box thread, while the extension that upper opening 607 raises upward is just right
Should be inserted into the slot with box thread, and be arranged on 607 lateral wall of upper opening between male thread and slot equipped with box thread into
Row cooperation, when safty shield 800 to be transferred in upper opening 607, can be realized installation between the two;In another example directly will
After safty shield 800 is placed in upper opening 607, bolt is set in 800 bottom surface surrounding of safty shield, is prevented safety with bolt
Connection, above-mentioned mounting means this field skill are installed between the bottom surface of shield 800 and the upper top surface of air rammer 600 to contact with each other
Art personnel combine the prior art to be fully able to realize, therefore this part of the present embodiment is not illustrated in figure.
Further, safty shield 800 further include cover 801, the linkage unit being set in cover 801 802 and
The overturning component 803 in 801 outside of cover is connect and is set to linkage unit 802, and linkage unit 802 and indicating arm 604 connect
It connecing, indicating arm 604 moves up and down with piston only 602, so that linkage unit 802 is driven to link, linkage unit
802 left-hand end and overturning component 803 are inconsistent, will overturn component 803 along with the movement of piston and contradict overturning, thus can also
It is enough in the movement travel of instruction piston.
More specifically, cover 801 is cylindrical shape, opens up on side wall and stretches out slot 801a, positioned at the upper of stretching slot 801a
Side's setting shutter 801b, shutter 801b are arranged at the longitudinal rail 801b-1 limit of 801 inner wall of cover, it is seen that
Longitudinal rail 801b-1 is the baffle of " L " type, can be located in guide rail and longitudinal sliding occurs, and the cross of shutter 801b
To width be greater than and stretch out slot 801a transverse notch width size, therefore when shutter 801b declines, can will stretch out slot 801a
The corresponding partial occlusion of notch effectively reduces dust and is entered in cover 801 by stretching slot 801a;And it is located at and stretches out slot 801a
Lower section inwardly along extended support plate 801c, be used to support linkage unit 802, which includes to extension bar
802a, lifter plate 802b, the first interlocking bar 802c, the second interlocking bar 802d and conflict idler wheel 802e, it should be noted that right
Extension bar 802a insertion 604 internal screw thread mode of indicating arm is installed, therefore is able to maintain synchronous up and down motion with indicating arm 604, should
Mounting means is with reference to the installation between safty shield 800 and upper opening 607, and those skilled in the art combine the signal of Fig. 7
It is not difficult to find that instruction can be inserted to extension bar 802a when safty shield 800 is embedded in and is rotatablely installed in upper opening 607
The rotational installation synchronized in bar 604, of course, it is possible to which the mode different by thread depth ratio setting, can be safety
Shield 800 is embedded in upper opening 607 and carries out after rotating certain distance, starts spiral shell between extension bar 802a and insertion indicating arm 604
Line cooperation is synchronous, can be achieved.Further, it is connected to the top of extension bar 802a with lifter plate 802b, to indicate
Bar 604 is able to maintain synchronous up and down motion to extension bar 802a and lifter plate 802b;First one end interlocking bar 802c passes through the
One axle bed 802c and lifter plate 802b are hinged, and one end of the other end and the second interlocking bar 802d is hinged by contradicting idler wheel 802e,
And second the other end of interlocking bar 802d pass through hinged between the second axle bed 802d-1 and support plate 801c, therefore work as indicating arm
604, extension bar 802a and lifter plate 802b are synchronized in the motion process being pressed downward, contradicts idler wheel 802e and is under pressure by stretching out
Slot 801a is stretched out and is contradicted to the inner wall of overturning component 803, and the process constantly pushed can contradict always overturning component 803 outward
Make its flip-over, when similarly moving upwards, contradicting idler wheel 802e can inwardly stretch, and overturning component 803 just not will receive outward
Conflict power.Further, overturning component 803 includes the torsional spring shaft 803a of bottom setting, it should be noted that torsional spring shaft
803a is using in the prior art with the shaft of spring torsion, in the present embodiment when contradicting idler wheel 802e and inwardly retracting, by turning round
Spring shaft 803a, which generates restoring force, makes to overturn component 803 with the trend to turn to the inside.
When under the present embodiment original state, illustrate for when valve is in the open state, when beginning, piston only 602
Above cavity 601, it should be noted that valve opening includes the two states for fully opening or not fully opening, is shown
Right, indicating arm 604 is in the distalmost end moved upwards on direction when fully opening, and it is understandable to be, when not fully opening
In half way, therefore the present embodiment, when valve fully opens, corresponding overturning component 803 is in a vertical state, and torsional spring turns
The spring of axis 803a is in the state that deformation occurs, and in order to which operator learns state at a glance, positioned at overturning component 803
Sign, such as the "ON" word that this implementation uses is arranged in lateral wall.
Further, it is moved gradually downward in piston only 602 and corresponds to valve 800 and progressively close off, while plug body 602
It moves downward and drives indicating arm 604, extension bar 802a and lifter plate 802b are moved downward, contradict idler wheel 802e at this time by under
Pressure is contradicted idler wheel 802e and is contradicted from the stretching for stretching out slot 801a to overturning group due to the hinged setting of each fulcrum of linkage unit 802
On the inner wall of part 803, it is downwardly turned over using torsional spring shaft 803a as fulcrum, the angle that overturning component 803 and cover 801 are constituted
It is continuously increased, deformation occurs for the spring in torsional spring shaft 803a, and overturning component 803 has the trend of revolution, and should work as in the process
The space that slot 801a is located above the first interlocking bar 802c is stretched out when first interlocking bar 802c declines will increase, and shutter 801b
It blocks the part that general who has surrendered stretches out that slot 801a is vacated under by gravity.Conversely, referring to when valve is by closing to unlatching demand
Show that bar 604 moves upwards, the revolution trend that overturning component 803 has is in a vertical state after fully opening.Likewise,
When first interlocking bar 802c rises, shutter 801b is contradicted, its is upward, therefore realize the rising of shutter 801b, from
And suitably reduces and fall volume dust granule in cover 801.According to above-mentioned those skilled in the art it is not difficult to find that can lead in the present embodiment
The size that the corresponding overturning component 803 of distance that indicating arm 604 rises or declines constitutes angle with cover 801 is crossed, indication valve is carried out
The degree that 800 valve plates of door are opened, for example, it is simplest after valve fully opens, and overturning component 803 is vertical, and the angle of composition is
0, and indicating arm 604 is in the distalmost end moved upwards, therefore can similarly obtain the feature of valve opening half vertically and arrive
Characteristic value when contract fully, similarly, the numerical value of the half of half it is also the same it is found that and so on, can be with user to valve
The actual needs of opening degree is calculated and carries out the instruction or rough instruction of specific value.
It should be noted that the above examples are only used to illustrate the technical scheme of the present invention and are not limiting, although referring to preferable
Embodiment describes the invention in detail, those skilled in the art should understand that, it can be to technology of the invention
Scheme is modified or replaced equivalently, and without departing from the spirit and scope of the technical solution of the present invention, should all be covered in this hair
In bright scope of the claims.
Claims (10)
1. a kind of multipurpose pVTt method gas flow standard device, it is characterised in that: including,
Volumetric standard group (100) comprising the volumetric standard of various criterion volume, the volumetric standard group (100) are divided into
0.1m3、3m3And 34m3The volumetric standard of normal volume specification is all made of overall skid-mounted structure setting on verification table position, and
Configure the constant guarantee component (101) of temperature;
Tong-test ammeter system (200) is set on mobile microscope carrier and connect with each volumetric standard group (100), Mei Gesuo
Detection work can be carried out independently or simultaneously by stating tong-test ammeter system (200);
Air supply system (300) is that the volumetric standard group (100) and the tong-test ammeter system (200) provide individual gas sources, also wraps
Positive pressure gas source (301) and negative pressure gas source (302) are included, the operation for being respectively used to positive pressure and vacuumizing;
Pipe-line system (400), for connecting the volumetric standard group (100), the tong-test ammeter system (200) and the gas source system
The flow path each pipeline composition united between (300), wherein the positive pressure gas source (301) and the negative pressure gas source (302) share it is a set of
The pipe-line system (400);And various criterion volume the volumetric standard group (100) and the tong-test ammeter system (200) altogether
With a set of air supply system (300).
2. multipurpose pVTt method gas flow standard device as described in claim 1, it is characterised in that: the verification table position is
For placing 34m3Volumetric standard platform position, corresponding carrying installation 34m3The volumetric standard group (100), and 34m3Standard is held
The constant guarantee component (101) of temperature of device group (100) configuration is set in constant temperature using water-jacket.
3. multipurpose pVTt method gas flow standard device as claimed in claim 1 or 2, it is characterised in that: the tong-test ammeter system
System (200) further includes tested nozzle (201) and standard scale (202), is connect between the two and the pipe-line system (400) using pipeline
Mounting means, each pipeline is respectively provided with measuring instrumentss;According to the principle of mass conservation, by the mass flow of standard scale and tested
The indicating value of table compares, and completes the detection of checklist.
4. multipurpose pVTt method gas flow standard device as claimed in claim 3, it is characterised in that: the pipe-line system
It (400) include main line (401) and manifold trunk branch (402);
The main line (401) is between the tong-test ammeter system (200), volumetric standard group (100), air supply system (300) three
Connection;The manifold trunk branch (402) is several branch lines on the main line (401), by the air supply system
(300) air pressure flow path branch.
5. claim 1,2 or 4 it is any as described in multipurpose pVTt method gas flow standard device, it is characterised in that: it is described
When negative pressure gas source (302) is the gas source of the volumetric standard group (100), device detection of negative pressure state comprising water ring vacuum pump
(302a) and sliding vane rotary vacuum pump (302b);When the positive pressure gas source (301) is the gas source of the volumetric standard group (100), device
For positive pressure detecting state, and the positive pressure gas source (301) includes air compressor, cooler, drying machine and different pressures
High pressure tank.
6. multipurpose pVTt method gas flow standard device as claimed in claim 5, it is characterised in that: further include that flow is adjusted
System and control system;
The flow control system and the volumetric standard group (100) are by the corresponding connection of pipeline, and the flow adjusts system
System includes the critical flow generating apparatus that flow is continuously adjusted, using the technology of continuous control critical flow nozzle flow;The control
System uses two-stage separate test and control system, is capable of the carrying out automatically controlling of complete paired systems, data acquisition, data processing, report
Management and record printing.
7. multipurpose pVTt method gas flow standard device as claimed in claim 6, it is characterised in that: the flow adjusts system
System further includes valve control assembly, under automatic Verification state, can select to switch corresponding valve by the control system
Door, and in place by the switch of limit switch guarantee valve, and valve control mode is pneumatic, electronic or surges.
8. multipurpose pVTt method gas flow standard device as claimed in claims 6 or 7, it is characterised in that: the control system
System includes host computer, slave computer, data acquisition and actuator;
The host computer control device operation and can stop in human-computer interaction interface set temperature value, flow value, and it is described on
Position machine, can be according to the generation pair of institute's measured data by the reception, transmission of data between Ethernet protocol realization and the slave computer
The probation redport of tested flowmeter;
The slave computer includes programmable controller PLC, A/D module and D/A module, and the A/D module is by temperature sensor, humidity
The analog signal that sensor, pressure sensor, flowmeter export is converted into digital data transmission to programmable controller PLC, reality
The acquisition of existing data;Digital signal is converted analog control signal output by the D/A module, realizes the control to the actuator
System.
9. multipurpose pVTt method gas flow standard device as claimed in claim 8, it is characterised in that: the data acquisition packet
Temperature sensor, humidity sensor, pressure sensor, proving flowmeter and tested flowmeter are included, above-mentioned output signal is mould
Quasi- signal;And the temperature sensor uses Pt100A grade platinum resistance, 0~50 DEG C, MPEV≤0.1 DEG C, scale division value is not more than
0.01℃;The pressure sensor uses 0.025 stage pressure transmitter;The humidity sensor uses digital display thermometer, measurement
Range: 10%~99%RH, allowable error ± 2%RH.
10. multipurpose pVTt method gas flow standard device as claimed in claim 9, it is characterised in that: the actuator with
The valve control assembly is corresponding, further includes pneumatic control valve door, frequency converter, power controller and thermo hydrograph regulator;
The signal that the frequency converter is exported by receiving PLC, controls the revolving speed of blower, the pneumatic control valve door passes through reception
Current analog signal adjusts aperture, and the two collective effect realizes the control to flow, the power controller and the temperature and humidity
For adjuster by receiving standard analog signal, gas temperature and the environment temperature control for controlling outflow heat exchanger respectively are indoor
Temperature.
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CN112082610A (en) * | 2020-08-11 | 2020-12-15 | 镇江市计量检定测试中心 | Standard container constant temperature device applied to pVTt method |
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