CN104677439A - Hydrogen gas flow rate detecting system and hydrogen gas flow rate detecting system - Google Patents
Hydrogen gas flow rate detecting system and hydrogen gas flow rate detecting system Download PDFInfo
- Publication number
- CN104677439A CN104677439A CN201310629907.XA CN201310629907A CN104677439A CN 104677439 A CN104677439 A CN 104677439A CN 201310629907 A CN201310629907 A CN 201310629907A CN 104677439 A CN104677439 A CN 104677439A
- Authority
- CN
- China
- Prior art keywords
- valve
- main line
- flow control
- open
- hydrogen
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Measuring Volume Flow (AREA)
Abstract
The invention discloses a hydrogen gas flow rate detecting system and a hydrogen gas flow detecting system. The system comprises a pressure reducing valve, a primary switch ball valve, a flow rate regulating valve, a flow rate regulating valve, a pressure sensor, a detected flow rate meter, a pressure sensor, a stagnation container opening-closing ball valve, a stagnation container, a sound speed spray nozzle, a pneumatic switch valve, an outlet container and a back-fire relief valve which are arranged on a high-pressure gas cylinder primary pipeline in sequence. The hydrogen gas flow rate detecting system can increase the detecting precision of the hydrogen gas and can reduce the measuring errors of the hydrogen gas consumption amount.
Description
Technical field
The present invention relates to field of flow detection, particularly a kind of hydrogen flowing quantity detection system and hydrogen flowing quantity detection method.
Background technology
Hydrogen with its cleanliness without any pollution, efficient, can store and transport, and the advantage such as wide material sources, be regarded as optimal energy carrier.Many experts and scholars think, consider from combined factors such as economy, technical, maneuverability and environmental friendliness features, and Hydrogen Energy is the power fuel of following most possible substitute fossil fuels.Hydrogen Energy and regenerative resource combine, by complete for formation one reproducible complete energy resource system.
Hydrogen flowing quantity detection method conventional at present utilizes flowmeter survey hydrogen flowing quantity, adopts flowmeter to measure the hydrogen flowing quantity flowed in fuel supply conduit continuously, draws hydrogen gas consumption.
But the hydrogen gas consumption error that this detection method draws is larger.
Summary of the invention
The embodiment of the present invention provides a kind of hydrogen flowing quantity detection system and hydrogen flowing quantity detection method, can improve the accuracy of detection of hydrogen, reduces hydrogen gas consumption measuring error.
The embodiment of the present invention adopts following technical scheme:
A kind of hydrogen flowing quantity detection system, comprising: be installed on the reduction valve on gas cylinder main line, main line switching ball, flow control valve, flow control valve, pressure transducer, tested flowmeter, pressure transducer, stagnation container valve ball valve, stagnation container, sonic nozzle, pneumatic on-off valve, exit vessel, spark arrester successively.
Optionally, setting pressure sensor, temperature sensor on described stagnation container.
Optionally, setting pressure sensor on described exit vessel.
Optionally, described gas cylinder main line installs at least one branch switch ball valve.
Optionally, flexible pipe is adopted to be connected between described gas cylinder with described reduction valve.
Optionally, described tested flowmeter is connected with the flexible pipe of described pressure sensor application ring flange interface.
The above-mentioned hydrogen flowing quantity detection system of a kind of application carries out hydrogen flowing quantity detection method, comprising:
Open main line valve, open flow control valve, open sonic nozzle pneumatic on-off valve, with purging bottle, rear closedown sonic nozzle pneumatic on-off valve is purged to whole pipeline, close flow control valve, close main line valve;
Open main line valve, open flow control valve, close sonic nozzle pneumatic on-off valve with after hydrogen purge pipeline, close flow control valve, close main line valve;
Open main line valve, open flow control valve, by reduction valve, stagnation container pressure is remained on more than 0.3Mpa with hydrogen;
Wait for that line-pressure sensor is consistent with stagnation container pressure, when measured stream gauge reading is 0, open sonic nozzle pneumatic on-off valve;
Measure hydrogen flowing quantity after flowmeter numerical stability, obtain measurement result.
Optionally, the calculating formula of described sonic nozzle measurement hydrogen quality flow is:
In formula:
Q
m---mass rate kg/s;
A
*---nozzle throat area of section m
2;
C---efflux coefficient;
C
*---actual gas critical flow;
P
0---the absolute stagnation pressure Pa of nozzle entrance place gas;
R---universal gas constant J/ (kmolK);
The molal weight kg/kmol of M---gas;
T
0---the absolute stagnation temperature K of gas;
A
*---determined by processing result or obtain through measuring.
Based on technique scheme, the hydrogen flowing quantity detection system of the embodiment of the present invention and hydrogen flowing quantity detection method, can improve the accuracy of detection of hydrogen, reduces hydrogen gas consumption measuring error.
Accompanying drawing explanation
In order to be illustrated more clearly in the embodiment of the present invention or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is some embodiments of the present invention, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
The structural representation of a kind of hydrogen flowing quantity detection system that Fig. 1 provides for the embodiment of the present invention 1.
In accompanying drawing: 1 is gas cylinder, 2 is gas cylinder main line, 3 is reduction valve, 4 is main line switching ball, 5 is flow control valve, 6 is flow control valve, 7 is pressure transducer, 8 is tested flowmeter, 9 is pressure transducer, 10 is stagnation container valve ball valve, 11 is temperature sensor, 12 is temperature sensor, 13 is pressure transducer, 14 is stagnation container, 15 is sonic nozzle, 16 is sonic nozzle, 17 is sonic nozzle, 18 is pneumatic on-off valve, 19 is pneumatic on-off valve, 20 is pneumatic on-off valve, 21 is exit vessel, 22 is pressure transducer, 23 is branch switch ball valve, 24 is branch switch ball valve, 25 is branch switch ball valve, 26 is spark arrester.
Embodiment
For making the object of the embodiment of the present invention, technical scheme and advantage clearly, below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly described, obviously, described embodiment is the present invention's part embodiment, instead of whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art, not making the every other embodiment obtained under creative work prerequisite, belong to the scope of protection of the invention.
Embodiment 1
As shown in Figure 1, the present embodiment provides a kind of hydrogen flowing quantity detection system, comprise: be installed on the reduction valve (3) on gas cylinder main line successively, main line switching ball (4), flow control valve (5), (6), pressure transducer (7), tested flowmeter (8), pressure transducer (9), stagnation container valve ball valve (10), stagnation container (14), sonic nozzle (15), sonic nozzle (16), sonic nozzle (17), pneumatic on-off valve (18), pneumatic on-off valve (19), pneumatic on-off valve (20), exit vessel (21) and spark arrester (26).
Wherein, in gas cylinder, hydrogen is housed, gas cylinder main line is used for exporting hydrogen from gas cylinder.
Optionally, stagnation container (14) is equipped with pressure transducer (13), temperature sensor (11), temperature sensor (12), exit vessel is equipped with pressure transducer (22).Main line is equipped with branch switch ball valve (27), branch switch ball valve (24), branch switch ball valve (25), gas in pipeline can be discharged by branch switch ball valve at any time.
Optionally, flexible pipe is adopted to be connected between gas cylinder (1) with reduction valve (3).
Optionally, the flexible pipe of ring flange interface is adopted to be connected between tested flowmeter (8) with pressure transducer (9).Flowmeter relies on Liftable base to support.
In the present embodiment, gas cylinder end adopts flexible pipe to connect, and can take into account different types of gas cylinder.There are two places' hand switch ball valve (4), (10) in trunk roads, can air feed be stopped under ensureing the emergency circumstance.Two flow control valves (5), (6) adopt and are connected in parallel, and ensure that more wide in range flow regulation is interval.Adopt flexible pipe to connect before and after flowmeter, be convenient for changing different types of flowmeter, pressure transducer (13) precision on stagnation container is 0.1%FS, and sample frequency reaches 10Hz, ensure that the accuracy of experiment.The method avoids the instability owing to causing meter readings after pressure variations influence stagnation container during unlatching gas cylinder (1) simultaneously.
In example of the present invention, first opened by high-pressure gas cylinder valve, open main line valve (4), (10), flow control valve (5), (6) aperture are 100%.Open three sonic nozzle pneumatic on-off valves (18), (19), (20), with purging bottle, purging is carried out to whole pipeline and after about 30 seconds, close three sonic nozzle pneumatic on-off valves (18), (19), (20) successively, flow control valve (5), (6) aperture are 0%, close main line valve (4), (10).Again open main line valve (4), (10) afterwards, now high pressure gas pressure of the inside of a bottle is 6.252Mpa, and flow control valve (5), (6) aperture are 100%, and in pipeline, pressure is 0.427Mpa, and stagnation container pressure is 0.43Mpa.Meter readings is 0.Open the sonic nozzle pneumatic on-off valve (20) needing to measure.Wait for that after about 80 seconds, flowmeter flow tends towards stability, start to record data, meter readings is obtained by flowmeter self communication, and sonic nozzle quality is according to calculating with the formula.
The hydrogen flowing quantity detection system of the present embodiment, can improve the accuracy of detection of hydrogen, reduces hydrogen gas consumption measuring error.
Embodiment 2
The present embodiment provides system described in a kind of Application Example 1 to carry out hydrogen flowing quantity detection method, comprising:
Open main line valve, open flow control valve, open sonic nozzle pneumatic on-off valve, with purging bottle, rear closedown sonic nozzle pneumatic on-off valve is purged to whole pipeline, close flow control valve, close main line valve;
Open main line valve, open flow control valve, close sonic nozzle pneumatic on-off valve with after hydrogen purge pipeline, close flow control valve, close main line valve;
Open main line valve, open flow control valve, by reduction valve, stagnation container pressure is remained on more than 0.3Mpa with hydrogen;
Wait for that line-pressure sensor is consistent with stagnation container pressure, when measured stream gauge reading is 0, open sonic nozzle pneumatic on-off valve;
Measure hydrogen flowing quantity after flowmeter numerical stability, obtain measurement result.
Optionally, the calculating formula of described sonic nozzle measurement hydrogen quality flow is:
In formula:
Q
m---mass rate kg/s;
A
*---nozzle throat area of section m
2;
C---efflux coefficient;
C
*---actual gas critical flow;
P
0---the absolute stagnation pressure Pa of nozzle entrance place gas;
R---universal gas constant J/ (kmolK);
The molal weight kg/kmol of M---gas;
T
0---the absolute stagnation temperature K of gas;
A
*---determined by processing result or obtain through measuring.
A is known quantity, is determined or try to achieve through measuring by processing result.
C has two kinds to ask method, and the experimental formula that the first provides according to ISO9300 calculates, and under the condition of the installation conformed with the regulations and request for utilization, the relative error of the efflux coefficient of trying to achieve like this is ± 0.5%, and the fiducial probability of this error is 95%.It two is asked for by standardization, requires to be arranged on gas flow standard device, survey out the gas mass flow flowing through nozzle, then go out efflux coefficient by above formula inverse by nozzle according to vertification regulation.
C
*according to the regulation of ISO9300, the method that available its accuracy any has been verified calculates, and for the critical flow of several conventional gas, can obtain by looking into the annex getting ISO9300.
P
0measure in nozzle upstream pressure, the position of its pressure tappings is chosen and pressure require should in accordance with the regulation of code.
R, to all gas, gets 8314.4.
M, to surveyed gas, can look into gas property table and obtain (molecular weight).
T
0measure in nozzle upstream, the position of its thermometer hole is chosen and thermometric require should in accordance with the regulation of code.
Beneficial effect of the present invention is: gas cylinder end adopts flexible pipe to connect, and can take into account different types of gas cylinder.There are two places' hand switch ball valve (4), (10) in trunk roads, can air feed be stopped under ensureing the emergency circumstance.Two flow control valves (5), (6) adopt and are connected in parallel, and ensure that more wide in range flow regulation is interval.Adopt flexible pipe to connect before and after flowmeter, be convenient for changing different types of flowmeter, pressure transducer (13) precision on stagnation container is 0.1%FS, and sample frequency reaches 10Hz, ensure that the accuracy of experiment.The method avoids the instability owing to causing meter readings after pressure variations influence stagnation container during unlatching gas cylinder (1) simultaneously.
Those skilled in the art can carry out various change and modification to the present invention and not depart from the spirit and scope of the present invention.Like this, if these amendments of the present invention and modification belong within the scope of the claims in the present invention and equivalent technologies thereof, then the present invention is also intended to comprise these change and modification.
Claims (8)
1. a hydrogen flowing quantity detection system, it is characterized in that, comprising: be installed on the reduction valve on gas cylinder main line, main line switching ball, flow control valve, flow control valve, pressure transducer, tested flowmeter, pressure transducer, stagnation container valve ball valve, stagnation container, sonic nozzle, pneumatic on-off valve, exit vessel, spark arrester successively.
2. system according to claim 1, is characterized in that, setting pressure sensor, temperature sensor on described stagnation container.
3. system according to claim 1, is characterized in that, setting pressure sensor on described exit vessel.
4. system according to claim 1, is characterized in that, described gas cylinder main line is installed at least one branch switch ball valve.
5. system according to claim 1, is characterized in that, adopts flexible pipe to be connected between described gas cylinder with described reduction valve.
6. system according to claim 1, is characterized in that, described tested flowmeter is connected with the flexible pipe of described pressure sensor application ring flange interface.
7. application rights requires that the hydrogen flowing quantity detection system according to any one of 1 to 6 carries out a hydrogen flowing quantity detection method, it is characterized in that, comprising:
Open main line valve, open flow control valve, open sonic nozzle pneumatic on-off valve, with purging bottle, rear closedown sonic nozzle pneumatic on-off valve is purged to whole pipeline, close flow control valve, close main line valve;
Open main line valve, open flow control valve, close sonic nozzle pneumatic on-off valve with after hydrogen purge pipeline, close flow control valve, close main line valve;
Open main line valve, open flow control valve, by reduction valve, stagnation container pressure is remained on more than 0.3Mpa with hydrogen;
Wait for that line-pressure sensor is consistent with stagnation container pressure, when measured stream gauge reading is 0, open sonic nozzle pneumatic on-off valve;
Measure hydrogen flowing quantity after flowmeter numerical stability, obtain measurement result.
8. method according to claim 7, is characterized in that, the calculating formula that described sonic nozzle measures hydrogen quality flow is:
In formula:
Q
m---mass rate kg/s;
A
*---nozzle throat area of section m
2;
C---efflux coefficient;
C
*---actual gas critical flow;
P
0---the absolute stagnation pressure Pa of nozzle entrance place gas;
R---universal gas constant J/ (kmolK);
The molal weight kg/kmol of M---gas;
T
0---the absolute stagnation temperature K of gas;
A
*---determined by processing result or obtain through measuring.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310629907.XA CN104677439A (en) | 2013-11-29 | 2013-11-29 | Hydrogen gas flow rate detecting system and hydrogen gas flow rate detecting system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310629907.XA CN104677439A (en) | 2013-11-29 | 2013-11-29 | Hydrogen gas flow rate detecting system and hydrogen gas flow rate detecting system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN104677439A true CN104677439A (en) | 2015-06-03 |
Family
ID=53312795
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310629907.XA Pending CN104677439A (en) | 2013-11-29 | 2013-11-29 | Hydrogen gas flow rate detecting system and hydrogen gas flow rate detecting system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104677439A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116335818A (en) * | 2023-01-02 | 2023-06-27 | 重庆长安汽车股份有限公司 | Hydrogen engine nozzle flow measuring device and measuring method |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20020193911A1 (en) * | 2001-06-13 | 2002-12-19 | Smc Kabushiki Kaisha | Mass flow rate-measuring method and mass flow rate control apparatus |
CN2814357Y (en) * | 2005-07-04 | 2006-09-06 | 西安佳禾资讯发展有限公司 | Sound speed nozzle gas flowmeter detector by barotropic process |
CN201225920Y (en) * | 2008-07-11 | 2009-04-22 | 河北省计量监督检测院 | Gas flow standard device combining acoustic speed nozzle method and standard table method |
CN101470020A (en) * | 2007-12-25 | 2009-07-01 | 清华大学 | Detection system and method for mesomeric state hydrogen gas consumption |
CN101782463A (en) * | 2009-01-15 | 2010-07-21 | 北京航空航天大学 | Full-flow test bed hydrogen system |
-
2013
- 2013-11-29 CN CN201310629907.XA patent/CN104677439A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20020193911A1 (en) * | 2001-06-13 | 2002-12-19 | Smc Kabushiki Kaisha | Mass flow rate-measuring method and mass flow rate control apparatus |
CN2814357Y (en) * | 2005-07-04 | 2006-09-06 | 西安佳禾资讯发展有限公司 | Sound speed nozzle gas flowmeter detector by barotropic process |
CN101470020A (en) * | 2007-12-25 | 2009-07-01 | 清华大学 | Detection system and method for mesomeric state hydrogen gas consumption |
CN201225920Y (en) * | 2008-07-11 | 2009-04-22 | 河北省计量监督检测院 | Gas flow standard device combining acoustic speed nozzle method and standard table method |
CN101782463A (en) * | 2009-01-15 | 2010-07-21 | 北京航空航天大学 | Full-flow test bed hydrogen system |
Non-Patent Citations (1)
Title |
---|
张宇飞: "燃料电池汽车氢气消耗量检测方法研究", 《中国优秀硕士学位论文全文数据库工程科技Ⅱ辑》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116335818A (en) * | 2023-01-02 | 2023-06-27 | 重庆长安汽车股份有限公司 | Hydrogen engine nozzle flow measuring device and measuring method |
CN116335818B (en) * | 2023-01-02 | 2024-05-14 | 重庆长安汽车股份有限公司 | Hydrogen engine nozzle flow measuring device and measuring method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2009290420B2 (en) | Method and device for detecting leaks in an underground liquid pipe, particularly a water pipe | |
CN104236816B (en) | A kind of leakage detecting instrument on-line calibration device and method | |
CN207081525U (en) | A kind of nuclear power station isolating valve reveals measurement apparatus | |
CN204881791U (en) | A capacity calibrating installation that is used for car tank wagon oil to exchange | |
KR20190038625A (en) | Method and apparatus for detecting the amount of gas in a calibratable manner | |
CN104677439A (en) | Hydrogen gas flow rate detecting system and hydrogen gas flow rate detecting system | |
CN204330095U (en) | Supercritical CO 2flowmeter prover | |
CN104122122B (en) | Pressure stability sampling apparatus | |
CN210774278U (en) | pVTt method gas flow standard device | |
CN106289372B (en) | Welded insulated gas cylinder Daily boil-off-rate measuring instrument test method | |
CN104568082A (en) | Supercritical CO2 flowmeter calibration device and calibration method thereof | |
CN102798420B (en) | A kind of method of testing of liquid loading and unloading process volatilization loss and system | |
CN104964724A (en) | Liquid storage tank evaporation rate measuring device and measuring method thereof | |
CN205261210U (en) | LNG loading sledge integrated device | |
CN206470284U (en) | The measurement apparatus of gas in pipelines flow velocity | |
CN111912584A (en) | Air tightness detection device for electric locomotive air supply system | |
CN104280529A (en) | Device and method for verifying flux of carbon dioxide, methane and nitrogen dioxide in soil | |
CN203881388U (en) | Oil gas flowmeter | |
CN109387265A (en) | Low temperature mass flowmenter performance testing device and method | |
JPS5533628A (en) | Testing and inspecting device of flow meter | |
CN202599631U (en) | Gas leakage detection system | |
CN203657893U (en) | Movable refueling machine determination device | |
CN205785652U (en) | A kind of device of detected air pressure | |
CN105781532B (en) | Leak source depth detection experimental device | |
CN206669335U (en) | A kind of CNG filling machines magnitude tracing system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20150603 |