A kind of gas liquid two purpose performance of safety valve assay device and test method
Technical field
The present invention relates to the assay device of the performance of safety valve of a set of gas liquid two purpose.
Background technology
Relief valve is last one overpressure protection apparatus of pressure bearing system, is main on boiler, pressure vessel, bearing pipe
Safety attachment.Therefore to ensure the quality of relief valve, all relief valve all must the property done in research and development and batch production process
Can test, to ensure that it meets standard-required.
Present relief valve divides according to Applicable media, can be divided into liquid safe valve and gas safety valve.And liquid peace
The performance of full valve needs liquid safe valve test bench location to go test, and gas safety valve needs gas safety valve test bench location to go
Test.This is the common situation of current all safety valve testing platform positions.And if a relief valve manufacturer produces two simultaneously
During the relief valve of type, also it is necessary for setting up liquid safe valve test bench location and gas safety valve testing table position respectively, so
Both occupy too much land area and too increase the cost of equipment construction.
Liquid safety valve test platform and the gaseous state safety valve test platform of present each relief valve producer are separately to build
If even some producer establishes the performance of safety valve test bench location that steam is special the most specially.But these test bench location
Function singleness.That is the test(ing) medium of air test platform position can only be compressed air;Liquid safe valve test bench location
Test(ing) medium can only be water.Two cover systems are incompatible.So will result in the most unnecessary waste: 1, two overlap test bench location
Need to hew out the place needed for two test bench location respectively, can not interfere, cause the waste in terms of occupation of land and building;
2, building two set test bench location, some equipment such as pressure vessel or compressor that originally can be general also must buy two sets,
So cause the waste of equipment;3, two test bench location are also required to safeguard respectively during one's term of military service, so also result in dimension
Protect the waste of cost;4, even will consider two set equipment power consumption simultaneously and water consumption in Factory Electricity Supply and water supply process, make
The waste that the capacity having become power supply water system increases and produces.
Summary of the invention
The technical problem to be solved in the present invention: use a test platform to complete liquid safety valve test and gaseous state safety
Valve is tested.
In order to solve above-mentioned technical problem, a technical scheme of the present invention there is provided a kind of safe valve actuation of gas liquid two purpose
Make performance test apparatus, it is characterised in that include compressor, pressure vessel one, pressure vessel two, pressure vessel three and pipeline system
System and control system, compressor communicates with pressure vessel two via valve one, and the gas outlet of pressure vessel two is successively via switch
Valve one, heavy caliber in parallel regulation valve one communicate with the air inlet of pressure vessel one with small-bore regulation valve one, switch valve two, pressure
Connecting on the drain of force container one has atmospheric valve one, tested gas safety valve to be connected with pressure vessel one via gate valve one,
It is connected on the same interface that gate valve one is connected with pressure vessel one and has bypass valve one;
Fluid to be measured relief valve connects pressure vessel three via gate valve two, same with what pressure vessel three was connected at gate valve two
Connecting on interface and have bypass valve two, the drain of pressure vessel three connects atmospheric valve two;The water filling port of pressure vessel two via
Hand stop valve one communicates with external water source, and the level measuring mouth of pressure vessel two connects liquidometer via hand stop valve two;
Pressure vessel three communicates with pressure vessel two via switch valve three, the gas outlet of pressure vessel one successively via switch valve four and
The heavy caliber regulation valve two of connection is connected with the air inlet of pressure vessel two with small-bore regulation valve two, switch valve five;
During gas test, pressure vessel one is test chamber, and pressure vessel two is as accumulator, at switch valve three
In closed mode, i.e. pressure vessel three is in idle state.But in liquid safe valve process of the test, pressure vessel one is storage
Energy device, pressure vessel container two is water storage pressure vessel, and pressure vessel three is test chamber.In order to ensure whole system safety
Valve runs reliably, and the design pressure of pressure vessel one, two, three is identical.
Switch valve one, heavy caliber regulation valve one, small-bore regulation valve one, switch valve two, atmospheric valve one, gate valve one, bypass
Valve one, switch valve three, gate valve two, bypass valve two, atmospheric valve two, switch valve four, heavy caliber regulation valve two small-bore regulation valve two,
Switch valve five is by control system;
Control system gathers tested gas safety valve, fluid to be measured relief valve, pressure vessel one, pressure vessel two, pressure
The related data of container three.The measurement of all data and acquisition precision and the requirement of control accuracy GB and ASME to be met.
Preferably, it is connected between described stop valve one with described pressure vessel two and has check-valves one;At described valve one
It is connected with between described pressure vessel two and has check-valves two.
Preferably, described pressure vessel one, described pressure vessel two, described pressure vessel three are respectively equipped with relief valve
One, relief valve two and relief valve three.
Preferably, the interface that described pressure vessel three is connected with described switch valve three is provided with valve two;In described pressure
The interface that force container two is connected with described switch valve three is provided with valve three;Described pressure vessel three connects and has valve four.
Preferably, described compressor is connected with described pressure vessel one via valve five and check-valves three successively.
Another technical scheme of the present invention there is provided a kind of based on above-mentioned gas liquid two purpose performance of safety valve examination
The gas safety valve set-pressure of experiment device and performance test method, it is characterised in that comprise the following steps:
Step 1, opening control, open valve one, switch valve one, heavy caliber regulation valve one, small-bore regulation valve one,
Switch valve two, other all valves are transferred to closed mode;
Step 2, start compressor, pressurize to lentamente pressure vessel two and pressure vessel one, when pressure vessel two and
When the pressure of pressure vessel one reaches 110% tested safety valve set pressure, it is ensured that have enough during regulation experiment
Source of the gas, stops boosting pressure vessel one;
Step 3, demarcate the initial value opening high test device of tested gas safety valve;
Step 4, somewhat unlatching bypass valve one, inflation in the pipeline between gate valve one and tested relief valve, until tested
Safety valve jumping up is the most qualified according to the tested relief valve of data analysis that control system collects, if pressure of adjusting does not meets rule
Fixed, then adjust spring pressure, until the compound regulation of continuous set-pressure;It is in course of adjustment and should make a record;
If the pressure of pressure vessel one exceedes the set-pressure of tested relief valve 115%, control system is by automatic safe
Switch valve one on chain closing presure container one admission line, switch valve two, and open atmospheric valve one, pressure vessel one pressure
When being down to tested relief valve 80% set-pressure, atmospheric valve one is closed in hand-reset;
Step 5, tested relief valve meet regulation after step 4 to be repeated a further three times, and carry out test data sheet, three weights
If the fluctuation range that the tested safety valve set pressure of gained is tested in retrial has beyond standard regulation, then continuation repetition step 4, otherwise,
Set-pressure has been tested;
After step 6, set-pressure have been tested, switch valve one, heavy caliber on closing presure container one inlet pipeline are adjusted
Joint valve one, small-bore regulation valve one, switch valve two;
Step 7, unlatching atmospheric valve one, when pressure vessel one pressure is down to tested relief valve 80% set-pressure, manually
Reset and close atmospheric valve one, open bypass valve one, after pressure balance, then fully open gate valve one, for testing tested relief valve
Performance is prepared;
Step 8, compressor continue to pressurize in pressure vessel two, after pressure reaches preset value, open pressure vessel one
The switch valve one of import department, switch valve two, slowly open the small-bore regulation valve one of pressure vessel one import department, continues pressure
Container one boosts to the 90% of tested safety valve set pressure;
Step 9, again demarcate tested relief valve and open high test device and the pressure test device of pressure vessel one;
Step 10, the heavy caliber regulation valve one opened on pressure vessel one inlet pipeline, controlling pressure vessel one is 103%
The set-pressure of tested relief valve, all pressure during whole and relief valve are opened high data and are acquired simultaneously;
If there is accident, pressure vessel one pressure exceedes tested relief valve 115% set-pressure, and control system will be automatically
Switch valve one on safety interlocking closing presure container one admission line, switch valve two, and open atmospheric valve one, pressure vessel one
When pressure is down to tested relief valve 80% set-pressure, atmospheric valve one is closed in hand-reset;
Step 11, when tested safety valve jumping up to specified height of opening, maintain stable emissions 3-5s, complete safety valve jumping up and steady
Determine emission testing, close small-bore regulation valve one, the most slowly close heavy caliber regulation valve one, record tested relief valve simultaneously
Return seat performance, after returning seat completely, completely close the switch valve one of pressure vessel one import, switch valve two and heavy caliber regulation valve
One, open atmospheric valve one afterwards, make pressure vessel one pressure drop to the set-pressure of tested relief valve of 80%;
Step 12, Treatment Analysis result of the test, according to tested relief valve each and test data, it may be judged whether continue to repeat
Again test until pass the test or scene determine termination test after testing or tested relief valve being carried out field adjustable;
Step 13, according to step 8 to step 12, complete other twice long run test, carry out deviation according to test data and divide
Analysis, if in the margin of tolerance of precision that specify in standard of the test data surveyed, being successfully completed test, otherwise termination test, analysis
Test separately after reason and adjustment.
Another technical scheme of the present invention there is provided a kind of based on above-mentioned gas liquid two purpose performance of safety valve examination
The liquid safe valve set-pressure of experiment device and performance test method, it is characterised in that comprise the steps:
Step 1, opening control, open switch valve three, and other all valves are transferred to closed mode;
Step 2, manual unlocking stop valve one and stop valve two, be filled with water to relief valve liquid pilot institute in pressure vessel two
The water level needed;
Step 3, open switch valve four, heavy caliber regulation valve two, small-bore regulation valve two, switch valve five, it is ensured that can give press
Force container one, pressure vessel two, pressure vessel San Tong method supercharging;
Step 4, startup compressor, pressurize to lentamente pressure vessel one, pressure vessel two, pressure vessel three, work as pressure
When the pressure of container one and pressure vessel three reaches 110% fluid to be measured safety valve set pressure, it is ensured that regulation experiment process
In have enough sources of the gas, stop pressure vessel three is boosted;
Step 5, the initial value opening high test device of demarcation fluid to be measured relief valve;
Step 6, somewhat unlatching bypass valve two, water-filling in the pipeline between gate valve two and fluid to be measured relief valve, until
Fluid to be measured safety valve jumping up, the most qualified according to the data analysis fluid to be measured relief valve that control system collects, if whole
Level pressure is against regulation, then adjust spring pressure, until the compound regulation of continuous set-pressure;Being in course of adjustment, it is easy to remember to do
Record;
If pressure vessel three pressure exceedes fluid to be measured relief valve 115% set-pressure, control system is by automatic safe
Switch valve four on chain closing presure container two admission line, switch valve five also open atmospheric valve two, pressure vessel three pressure
When being down to fluid to be measured relief valve 80% set-pressure, atmospheric valve two is closed in hand-reset;
Step 7, fluid to be measured relief valve meet regulation after step 6 to be repeated a further three times, and carry out test data sheet, three
If the secondary fluctuation range repeating to test gained safety valve set pressure has beyond standard regulation, then continuation repetition step 6, otherwise,
Set-pressure has been tested;
After step 8, set-pressure have been tested, switch valve four on closing presure container two inlet pipeline, switch valve five,
Heavy caliber regulation valve two, small-bore regulation valve two;
Step 9, unlatching atmospheric valve two, be down to fluid to be measured relief valve the pressure in pressure vessel three and pressure vessel two
During 80% set-pressure, quick release valve two is closed in hand-reset, opens bypass valve two, after pressure balance, then fully opens
Gate valve two, prepares for test performance of safety valve;
Step 10, compressor continue to pressurize, after pressure reaches preset value in pressure vessel one.Open pressure vessel two
The switch valve four of import department, switch valve five, slowly open the small-bore regulation valve two of test chamber import department, continues to hold pressure
Device three and pressure vessel two boost to the 90% of fluid to be measured safety valve set pressure;
The stress test dress opening high test device and pressure vessel three of step 11, again demarcation fluid to be measured relief valve
Put;
Step 12, the heavy caliber regulation valve two opened on pressure vessel triple feed inlet pipeline, controlling pressure vessel three pressure is
The set-pressure of the fluid to be measured relief valve of 103%, simultaneously opens all pressure during whole and relief valve high data and carries out
Gather;
If pressure vessel three pressure exceedes fluid to be measured relief valve 115% set-pressure, control system is by automatic safe
Switch valve four on chain closing presure container two admission line, switch valve five, and open atmospheric valve two, pressure vessel three pressure
When being down to fluid to be measured relief valve 80% set-pressure, atmospheric valve two is closed in hand-reset;
Step 13, when fluid to be measured safety valve jumping up to specified height of opening, maintain stable emissions 3-5s, complete safety valve jumping up
And stable emissions test, the small-bore regulation valve two in closing presure container two air inlet pipe, the most slowly close heavy caliber regulation
Valve two, simultaneously time seat performance of record security valve, after returning seat completely, the switch valve four of complete pressure vessel two import, switch valve
Five and heavy caliber regulation valve two, open atmospheric valve two afterwards, make pressure vessel three pressure drop to the fluid to be measured relief valve of 80%
Set-pressure;
Step 14, Treatment Analysis result of the test, according to safety valve product each and test data, it may be judged whether continue to repeat
Again test until pass the test or scene determine termination test after testing or relief valve being carried out field adjustable;
Step 15, according to step 10 to step 14, complete other twice long run test, carry out deviation according to test data and divide
Analysis, if in the margin of tolerance of precision that specify in standard of the test data surveyed, being successfully completed test, otherwise termination test, analysis
Test separately after reason and adjustment.
The present invention is organically combined togather liquid and air-safety valve events performance test stand position, and is this safety
The corresponding operation technological process of valve pilot system tailor.This sets of plan effectively overcome before gas and liquid safe valve
Test bench location separately design and the defect built, be greatly saved construction land, equipment investment, factory's distribution and maintenance cost
Deng.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the present invention, and in figure, circle horizontal line represents that data acquisition line concentration, transverse line represent control line, and signal is all
Sent by the computer in figure or gathered.
Detailed description of the invention
For making the present invention become apparent, hereby with preferred embodiment, and accompanying drawing is coordinated to be described in detail below.
In conjunction with Fig. 1, a kind of gas liquid two purpose performance of safety valve assay device that the present invention provides includes compressor 1, pressure
Force container 1, pressure vessel 23, pressure vessel 34 and control system 28, pressure vessel 1, pressure vessel 23, pressure hold
Relief valve 1, relief valve 2 13 and relief valve 3 31 it is respectively equipped with on device 34.Pressure vessel 34 connects and has valve four
36
Compressor 1 communicates with pressure vessel 23 via valve 1, check-valves 28, and the gas outlet of pressure vessel 23 is successively
Via switch valve 1, heavy caliber in parallel regulation valve 1 and small-bore regulation valve 1, switch valve 2 23 and pressure vessel
The air inlet of 1 communicates, and the drain of pressure vessel 1 connects atmospheric valve 1, and tested relief valve 25 is via gate valve one
26 are connected with pressure vessel 1, and being connected on the same interface that gate valve 1 is connected with pressure vessel 1 has bypass valve 1;
Fluid to be measured relief valve 34 connects pressure vessel 34 via gate valve 2 33, in gate valve 2 33 and pressure vessel 34 phase
Connecting on same interface even and have bypass valve 2 32, the drain of pressure vessel 34 connects atmospheric valve 2 35;Pressure vessel two
The water filling port of 3 communicates with fire hydrant 16 via check-valves 1, stop valve 1, the level measuring mouth of pressure vessel 23 via
Stop valve 2 18 connects liquidometer 17;Pressure vessel 34 communicates with pressure vessel 23 via switch valve 3 29, at pressure vessel
34 interfaces being connected with switch valve 3 29 are provided with valve 2 30, on the interface that pressure vessel 23 is connected with switch valve 3 29
It is provided with valve 3 19;The gas outlet of pressure vessel 1 regulates valve 2 10 with little via switch valve 49, heavy caliber in parallel successively
Bore regulation valve 2 11, switch valve 5 12 are connected with the air inlet of pressure vessel 23;
Compressor 1 is connected with pressure vessel 1 via valve 55 and check-valves 37 the most successively;
Switch valve 1, heavy caliber regulation valve 1, small-bore regulation valve 1, switch valve 2 23, atmospheric valve 1, lock
Valve 1, bypass valve 1, switch valve 3 29, gate valve 2 33, bypass valve 2 32, atmospheric valve 2 35, switch valve 49, heavy caliber
Regulation valve 2 10 small-bore regulation valve 2 11, switch valve 5 12 are by control system 28;
Control system 28 gathers tested relief valve 25, fluid to be measured relief valve 34, bypass valve 1, bypass valve 2 32, pressure
Force container 1, pressure vessel 23, the data of pressure vessel 34.
During gas test, pressure vessel 1 is test chamber, and pressure vessel 23 is as accumulator, switch valve three
29 are closed, i.e. pressure vessel 34 is in idle state.But in liquid safe valve process of the test, pressure vessel
One 2 is accumulator, and pressure vessel 23 is water storage bulk container, and pressure vessel 34 is test chamber.In order to ensure whole system
Relief valve runs reliably, pressure vessel 1, pressure vessel 23, pressure vessel 34 design pressure identical.
A kind of gas safety valve set-pressure of present invention offer and performance test method, comprise the following steps:
Step 1, opening control 28, open valve 1, switch valve 1, heavy caliber regulation valve 1, small-bore tune
Joint valve 1, switch valve 2 23, other all valves are transferred to closed mode;
Step 2, startup compressor 1, give pressure vessel 23 and pressure vessel 1 pressurization, lentamente when pressure vessel 23
And the pressure of pressure vessel 1 is when reaching 110% tested safety valve set pressure, it is ensured that have the most sufficient during regulation experiment
Enough sources of the gas, stop boosting pressure vessel 1;
Step 3, demarcate the initial value opening high test device of tested relief valve 25;
Step 4, somewhat unlatching bypass valve 1, inflation in the pipeline between gate valve 1 and tested relief valve 25, directly
To the take-off of tested relief valve 25, the most qualified according to the data analysis tested relief valve 25 that control system 28 collects, if whole
Level pressure is against regulation, then adjust spring pressure, until the compound regulation of continuous set-pressure;Being in course of adjustment, it is easy to remember to do
Record;
If the pressure of pressure vessel 1 exceedes the set-pressure of tested relief valve 25115%, control system 28 will be automatically
Switch valve 1 on safety interlocking closing presure container 1 admission line, switch valve 2 23, and open atmospheric valve 1, pressure
When force container 1 pressure is down to tested relief valve 2580% set-pressure, atmospheric valve 1 is closed in hand-reset;
Step 5, tested relief valve 25 meet regulation after step 4 to be repeated a further three times, and carry out test data sheet, three times
If the fluctuation range repeating to test gained tested relief valve 25 set-pressure has beyond standard regulation, then continue to repeat step 4, no
Then, set-pressure has been tested;
After step 6, set-pressure have been tested, the switch valve 1 on closing presure container 1 inlet pipeline, heavy caliber
Regulation valve 1, small-bore regulation valve 1, switch valve 2 23;
Step 7, unlatching atmospheric valve 1, when pressure vessel 1 pressure is down to tested relief valve 2580% set-pressure,
Atmospheric valve 1 is closed in hand-reset, opens bypass valve 1, after pressure balance, then fully opens gate valve 1, for test
Tested relief valve 25 performance is prepared;
Step 8, compressor 1 continue to pressurize in pressure vessel 23, after pressure reaches preset value, open pressure vessel
The switch valve 1 of one 2 import departments, switch valve 2 23, slowly open the small-bore regulation valve 1 of pressure vessel 1 import department,
Continue pressure vessel 1 is boosted to the 90% of tested relief valve 25 set-pressure;
Step 9, again demarcate tested relief valve 25 and open high test device and the pressure test device of pressure vessel 1;
Step 10, the heavy caliber regulation valve 1 opened on pressure vessel 1 inlet pipeline, controlling pressure vessel 1 is
The set-pressure of the tested relief valve 25 of 103%, simultaneously opens all pressure during whole and relief valve high data and adopts
Collection;
If there is accident, pressure vessel 1 pressure exceedes tested relief valve 25115% set-pressure, control system 28
By the switch valve 1 on chain for automatic safe closing presure container 1 admission line, switch valve 2 23, and open atmospheric valve one
37, when pressure vessel 1 pressure is down to tested relief valve 2580% set-pressure, atmospheric valve 1 is closed in hand-reset;
Step 11, when tested relief valve 25 jumps to specified height of opening, maintain stable emissions 3-5s, complete safety valve jumping up and
Stable emissions is tested, and closes small-bore regulation valve 1, the most slowly closes heavy caliber regulation valve 1, records tested peace simultaneously
Time seat performance of full valve 25, after returning seat completely, completely closes the switch valve 1 of pressure vessel 1 import, switch valve 2 23 and
Heavy caliber regulation valve 1, opens atmospheric valve 1 afterwards, makes pressure vessel 1 pressure drop to the tested relief valve 25 of 80%
Set-pressure;
Step 12, Treatment Analysis result of the test, according to tested relief valve 25 each and test data, it may be judged whether continue weight
Retrial is tested again until pass the test or scene determine termination test after testing or tested relief valve 25 carrying out field adjustable;
Step 13, according to step 8 to step 12, complete other twice long run test, carry out deviation according to test data and divide
Analysis, if in the margin of tolerance of precision that specify in standard of the test data surveyed, being successfully completed test, otherwise termination test, analysis
Test separately after reason and adjustment.
A kind of liquid safe valve set-pressure of present invention offer and performance test method, comprise the steps:
Step 1, opening control 28, open switch valve 3 29, and other all valves are transferred to closed mode;
Step 2, manual unlocking stop valve 1 and stop valve 2 18, be filled with water to relief valve liquid in pressure vessel 23
Water level required for test;
Step 3, open switch valve 49, heavy caliber regulation valve 2 10, small-bore regulation valve 2 11, switch valve 5 12, it is ensured that
The supercharging simultaneously of pressure vessel 1, pressure vessel 23, pressure vessel 34 can be given;
Step 4, startup compressor 1, give the pressurization of pressure vessel 1, pressure vessel 23, pressure vessel 34 lentamente, when
When the pressure of pressure vessel 1 and pressure vessel 34 reaches 110% fluid to be measured relief valve 34 set-pressure, it is ensured that adjust
Process of the test has enough sources of the gas, stops pressure vessel 34 is boosted;
Step 5, the initial value opening high test device of demarcation fluid to be measured relief valve 34;
Step 6, somewhat unlatching bypass valve 2 32, fill in the pipeline between gate valve 2 33 and fluid to be measured relief valve 34
Gas, until fluid to be measured relief valve 34 take-off, according to the data analysis fluid to be measured relief valve 34 that control system 28 collects be
No qualified, if pressure of adjusting is against regulation, then adjust spring pressure, until the compound regulation of continuous set-pressure;Adjusting
Cheng Zhongying makes a record;
If pressure vessel 34 pressure exceedes fluid to be measured relief valve 34115% set-pressure, control system 28 will be automatically
Switch valve 49 on safety interlocking closing presure container 23 admission line, switch valve 5 12 also open atmospheric valve 2 35, pressure
When container 34 pressure is down to fluid to be measured relief valve 3480% set-pressure, atmospheric valve 2 35 is closed in hand-reset;
Step 7, fluid to be measured relief valve 34 meet regulation after step 6 to be repeated a further three times, and carry out test data sheet,
If the fluctuation range repeating to test gained safety valve set pressure for three times has beyond standard regulation, then continue to repeat step 6, no
Then, set-pressure has been tested;
After step 8, set-pressure have been tested, the switch valve 49 on closing presure container 23 inlet pipeline, switch valve
5 12, heavy caliber regulation valve 2 10, small-bore regulation valve 2 11;
Step 9, unlatching atmospheric valve 2 35, be down to fluid to be measured peace the pressure in pressure vessel 34 and pressure vessel 23
During full valve 3480% set-pressure, quick release valve 2 35 is closed in hand-reset, opens bypass valve 2 32, after pressure balance,
Fully open gate valve 2 33 again, prepare for test performance of safety valve;
Step 10, compressor 1 continue to pressurize, after pressure reaches preset value in pressure vessel 1.Open pressure vessel
The switch valve 49 of 23 import departments, switch valve 5 12, slowly open the small-bore regulation valve 2 11 of test chamber import department, continues
Pressure vessel 34 and pressure vessel 23 are boosted to the 90% of fluid to be measured relief valve 34 set-pressure;
The height of opening of step 11, again fluid to be measured relief valve 34 tests device and the pressure test device of pressure vessel 34;
Step 12, the heavy caliber regulation valve 2 10 opened on pressure vessel 34 inlet pipeline, control pressure vessel 34 pressure
Power is the set-pressure of the fluid to be measured relief valve 34 of 103%, simultaneously all pressure during whole and relief valve is opened high number
According to being acquired;
If pressure vessel 34 pressure exceedes fluid to be measured relief valve 34115% set-pressure, control system 28 will be automatically
Switch valve 49 on safety interlocking closing presure container 23 admission line, switch valve 5 12, and open atmospheric valve 2 35, pressure
When container 34 pressure is down to fluid to be measured relief valve 3480% set-pressure, atmospheric valve 2 35 is closed in hand-reset;
Step 13, when fluid to be measured relief valve 34 jumps to specified height of opening, maintain stable emissions 3-5s, complete relief valve and rise
Jump and stable emissions test, the small-bore regulation valve 2 11 in closing presure container 23 air inlet pipe, slowly close heavy caliber simultaneously
Regulation valve 2 10, simultaneously time seat performance of record security valve, after returning seat completely, the switch valve four of complete pressure vessel 23 import
9, switch valve 5 12 and heavy caliber regulation valve 2 10, open atmospheric valve 2 35 afterwards, make pressure vessel 34 pressure drop to 80%
The set-pressure of fluid to be measured relief valve 34;
Step 14, Treatment Analysis result of the test, according to safety valve product each and test data, it may be judged whether continue to repeat
Again test until pass the test or scene determine termination test after testing or relief valve being carried out field adjustable;
Step 15, according to step 10 to step 14, complete other twice long run test, carry out deviation according to test data and divide
Analysis, if in the margin of tolerance of precision that specify in standard of the test data surveyed, being successfully completed test, otherwise termination test, analysis
Test separately after reason and adjustment.