CN106482973A - Plate type heat exchanger liquid phase medium pressure fall-off test system and its method of testing - Google Patents

Plate type heat exchanger liquid phase medium pressure fall-off test system and its method of testing Download PDF

Info

Publication number
CN106482973A
CN106482973A CN201611029975.2A CN201611029975A CN106482973A CN 106482973 A CN106482973 A CN 106482973A CN 201611029975 A CN201611029975 A CN 201611029975A CN 106482973 A CN106482973 A CN 106482973A
Authority
CN
China
Prior art keywords
pressure
heat exchanger
pipeline section
circulation
plate type
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.)
Granted
Application number
CN201611029975.2A
Other languages
Chinese (zh)
Other versions
CN106482973B (en
Inventor
崔云龙
张中清
闫永超
彭小敏
何颜红
张�杰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Gansu Boiler Pressure Vessel Inspection Inst
Hefei General Machinery Research Institute Co Ltd
Original Assignee
Gansu Boiler Pressure Vessel Inspection Inst
Hefei General Machinery Research Institute Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Gansu Boiler Pressure Vessel Inspection Inst, Hefei General Machinery Research Institute Co Ltd filed Critical Gansu Boiler Pressure Vessel Inspection Inst
Priority to CN201611029975.2A priority Critical patent/CN106482973B/en
Publication of CN106482973A publication Critical patent/CN106482973A/en
Application granted granted Critical
Publication of CN106482973B publication Critical patent/CN106482973B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01MTESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
    • G01M99/00Subject matter not provided for in other groups of this subclass

Landscapes

  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Examining Or Testing Airtightness (AREA)
  • Investigating Or Analyzing Materials Using Thermal Means (AREA)

Abstract

The present invention relates to a kind of plate type heat exchanger liquid phase medium pressure fall-off test system.This test system includes tank case and plate type heat exchanger, the liquid test pipeline section that gone out by the test of first circulation feed liquor pipeline section, first circulation being communicated between tank case and plate type heat exchanger each other constitutes first circulation loop, and goes out liquid test pipeline section by second circulation feed liquor test pipeline section, second circulation and constitute second circulation loop;Working medium conveyor module and Flow-rate adjustment module are provided with first circulation feed liquor test pipeline section and second circulation feed liquor test pipeline section;Plate type heat exchanger is provided with pressure measuring module with four interfaces of closed circuit;Exhaust module is additionally provided with first circulation loop and second circulation loop.Present invention also offers the three kinds of method of testings matched with this test system.Present system simple structure, regulation are quick and convenient, and coverage test scope is wide.The present invention can effectively improve impact of the plate deformation factor to measurement result on the premise of pressure fall-off test technological requirement is met.

Description

Plate type heat exchanger liquid phase medium pressure fall-off test system and its method of testing
Technical field
The invention belongs to heat exchanger performance analysis and test control technology field, and in particular to a kind of plate type heat exchanger liquid phase Media pressure drop test system and its method of testing.
Background technology
The pressure drop that liquid phase medium flow resistance causes in plate type heat exchanger, is that of its economical operation effect of differentiation is important Factor.The exploitation and existing product power demand in technological process that plate type heat exchanger pressure fall-off test is worked as heat exchanger new product Determination, reliable data supporting is provided.As Large Plate Heat Exchangers are in the extensive application of nuclear power field, plate size is more next Bigger, plate more and more thinner, during actual test, plate Light deformation problem brings considerable influence to test result.
At present, the test system of plate type heat exchanger liquid phase medium flow resistance is mainly according to standard《JB/T10379》In " liquid-liquid measurement system " as shown in Figure 1 is set up.The system is mainly used in plate type heat exchanger thermal performance test, while also may be used Carry out pressure drop performance test.Plate type heat exchanger is warm, cold media of both sides interface is respectively connected to corresponding autonomous system pipeline, each other Wu dry Disturb.Particularly, the plate type heat exchanger d in Fig. 1 cold medium outlet by pipeline be sequentially connected cooler c, cooling tower b and Liquid storage vessel a, constitutes cold medium loop finally by cold medium pump is connected with cold medium import;Plate type heat exchanger d in Fig. 1 Thermal medium outlet liquid storage vessel, thermal medium pump are sequentially connected by pipeline, be connected with thermal medium entrance finally by heater e And constitute thermal medium loop.Cold medium loop and thermal medium loop in Fig. 1 is two not joining independent pipelines each other System.
But for the only user of pressure fall-off test demand, such test system because include temperature control modules, Technique is relative complex, and cost of investment is high, and floor space is wide;And during actual test, because of the not clear and definite pressure fall-off test side of standard Case, exist both sides working medium sequencing flow into plate type heat exchanger, plate type heat exchanger both sides tunnel inlets pressure differential larger situations such as, The pressurized Light deformation of heat exchange plate is caused, this brings very important impact to plate type heat exchanger pressure fall-off test result.
Content of the invention
In order to solve above-mentioned technical problem, an object of the present invention there is provided a kind of plate type heat exchanger liquid phase medium pressure Drop test system, this test system on the premise of pressure fall-off test technological requirement is met, effectively can improve plate deformation because Impact of the element to measurement result, while investment reduction cost.
In order to the purpose of the present invention is realized, technical scheme below is present invention employs:
A kind of plate type heat exchanger liquid phase medium pressure fall-off test system, including tank case and plate type heat exchanger, the tank case and plate The connection test of first circulation feed liquor pipeline section, first circulation each other is provided between formula heat exchanger goes out liquid test pipeline section and second Circulation feed liquor test pipeline section, second circulation go out liquid test pipeline section, and the first circulation feed liquor test pipeline section, first circulation go out liquid survey Test tube section constitutes first circulation loop, and the second circulation feed liquor test pipeline section, second circulation go out liquid test pipeline section and constitute second Closed circuit;
Working medium conveyor module is provided with the first circulation feed liquor test pipeline section and second circulation feed liquor test pipeline section With Flow-rate adjustment module;
First circulation feed liquor test pipeline section, first circulation go out liquid test pipeline section, second circulation feed liquor test pipeline section, the Two recycle liquid test pipeline section is provided with pressure measuring module with the junction of plate type heat exchanger;
This test system is also arranged on the respective at least one test pipeline section in first circulation loop and second circulation loop There is exhaust module.
Preferably, the caliber and pipeline of the first circulation feed liquor test pipeline section and second circulation feed liquor test pipeline section are long Degree correspondent equal, first circulation go out caliber and the length of pipe correspondence phase that liquid test pipeline section, second circulation go out liquid test pipeline section Deng;Working medium conveyor module and Flow-rate adjustment module are on first circulation feed liquor test pipeline section and second circulation feed liquor test pipeline section Installation site correspondence is identical, and the model correspondence of corresponding component is identical.
Preferably, the working medium conveyor module be arranged on first circulation feed liquor test pipeline section on the first variable frequency pump and The second variable frequency pump being arranged on second circulation feed liquor test pipeline section.
It is further preferred that the Flow-rate adjustment module be arranged on first circulation feed liquor test pipeline section on from tank case extremely The first flowmeter and the first regulating valve of plate type heat exchanger order arrangement, and for being arranged on second circulation feed liquor test pipeline section The second flowmeter that arranges from tank case to plate type heat exchanger order and the second regulating valve;First variable frequency pump is arranged on tank case On first circulation feed liquor test pipeline section between first flowmeter, second variable frequency pump is arranged on tank case and second flowmeter Between second circulation feed liquor test pipeline section on.
Preferably, the pressure measuring module is pressure transmitter.
Preferably, the exhaust module is to be arranged on the first row air valve that first circulation goes out on liquid test pipeline section, Yi Jishe Put second circulation go out liquid test pipeline section on second row air valve, the first row air valve first circulation go out liquid test pipeline section and The installation site that second row air valve goes out on liquid test pipeline section in second circulation corresponds to identical.
It is further preferred that this test system also includes pressure balance module, the pressure balance module includes to connect One circulation feed liquor test pipeline section and second circulation feed liquor test the pressure-equalizing pipe of pipeline section, the pressure-equalizing pipe and first circulation Feed liquor test pipeline section junction be arranged on first circulation feed liquor test pipeline section on pressure measuring module and the first regulating valve it Between, the pressure-equalizing pipe is arranged on second circulation feed liquor test pipeline section with the junction of second circulation feed liquor test pipeline section Between pressure measuring module and the second regulating valve;The pressure-equalizing pipe is on the pipe shaft near first circulation feed liquor test pipeline section The first balanced valve is provided with, it is flat that the pressure-equalizing pipe is provided with second on the pipe shaft near second circulation feed liquor test pipeline section Weighing apparatus valve.
The second object of the present invention provides a kind of method of testing using above-mentioned test system, and method of testing has three skills Art scheme, difference are as follows:
First technical scheme:A kind of method of testing using aforementioned plate type heat exchanger liquid phase medium pressure fall-off test system, Plate type heat exchanger be respectively connected with the working medium in logical two passage for uniform flow with first circulation loop and second circulation loop Flowing, this method of testing comprise the steps:
S1, the cutting-off valve being first turned on first circulation loop and second circulation loop, start the first variable frequency pump and the Two variable frequency pumps, the first regulating valve of standard-sized sheet and the second regulating valve, open first row air valve, second row air valve, in pipeline to be drained After fixed gas, first row air valve, second row air valve is closed;
The flow signal of S2, collection first flowmeter and second flowmeter, adjusts the first variable frequency pump, the second frequency conversion pump work Rate, after stability of flow in pipeline, requires according to plate type heat exchanger both sides channel capacity, changes according to first flowmeter flow signal Become the first control valve opening, change the second control valve opening according to second flowmeter flow signal, to meet in two closed circuits Operating mode traffic requirement;
After S3, operating condition of test are stable, the plate that four pressure transmitter measurements are obtained is recorded by plc data acquisition controller Formula exchanger heat side-entrance pressure Phi, plate type heat exchanger hot side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, Plate type heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger drooping characteristic is respectively by pressure Phi, pressure Pho, pressure Pci, pressure Power Pco is calculated;
In step S1, S2, first variable frequency pump and the second frequency conversion pump startup and the Flow-rate adjustment in two closed circuits will Synchronously carry out.
Second technical scheme:A kind of method of testing using aforementioned plate type heat exchanger liquid phase medium pressure fall-off test system, The working medium that the passage that plate type heat exchanger is connected with a loop in two closed circuits is flowed in wing passage is in flowing State, is full of working medium in the passage that plate type heat exchanger is connected with another loop i.e. topping up pressurize wing passage and working medium does not flow Dynamic, the flowing wing passage of plate type heat exchanger is identical with the working medium hydraulic pressure in topping up pressurize wing passage;
This method of testing is provided with pressure balance module in a test system, and the pressure balance module includes to connect first Circulation feed liquor test pipeline section and second circulation feed liquor test the pressure-equalizing pipe of pipeline section, and the pressure-equalizing pipe is entered with first circulation The junction of liquid test pipeline section is arranged between the pressure measuring module on first circulation feed liquor test pipeline section and the first regulating valve, The pressure-equalizing pipe is arranged on the pressure on second circulation feed liquor test pipeline section with the junction of second circulation feed liquor test pipeline section Between power measurement module and the second regulating valve;The pressure-equalizing pipe is set on the pipe shaft near first circulation feed liquor test pipeline section The first balanced valve is equipped with, the pressure-equalizing pipe is provided with the second balance on the pipe shaft near second circulation feed liquor test pipeline section Valve.
This method of testing comprises the steps:
S1, the cutting-off valve that opens on the closed circuit being connected with flowing wing passage, are made and topping up pressurize wing passage phase Cutting-off valve on the closed circuit of connection is remained off, the tune on closed circuit that standard-sized sheet is connected with flowing wing passage Section valve, opens the first balanced valve and the second balanced valve, makes the flowing wing passage in plate type heat exchanger and topping up pressurize wing passage phase Connection;Start the variable frequency pump on the closed circuit being connected with flowing wing passage, open the air bleeding valve on this closed circuit, the row for the treatment of After fixed gas to the greatest extent in this closed circuit, the air bleeding valve closed on this closed circuit;
The flow signal of the flowmeter on closed circuit that S2, collection are connected with flowing wing passage, adjusts this and loops back Frequency conversion pump power on road, after the working medium flow in this closed circuit is stable, will according to plate type heat exchanger one side channel capacity Ask, change the regulation on this closed circuit according to the flow signal of the flowmeter on the closed circuit being connected with flowing wing passage Valve opening, to meet the side operating mode traffic requirement;
After S3, operating condition of test are stable, the plate that four pressure transmitter measurements are obtained is recorded by plc data acquisition controller Formula exchanger heat side-entrance pressure Phi, plate type heat exchanger hot side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, Plate type heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger drooping characteristic is respectively by pressure Phi, pressure Pho, pressure Pci, pressure Power Pco is calculated;
3rd technical scheme:A kind of method of testing using aforementioned plate type heat exchanger liquid phase medium pressure fall-off test system, The working medium that the passage that plate type heat exchanger is connected with a loop in two closed circuits is flowed in wing passage is in flowing State, another passage of plate type heat exchanger is that empty liquid normal pressure wing passage is communicated with air;This method of testing comprises the steps:
S1, the cutting-off valve that opens on the closed circuit being connected with flowing wing passage, standard-sized sheet are connected with flowing wing passage Regulating valve on logical closed circuit;Start the variable frequency pump on the closed circuit being connected with flowing wing passage, open this circulation Air bleeding valve on loop, after the fixed gas in this closed circuit is drained, the air bleeding valve closed on this closed circuit;
The cutting-off valve that closes on the closed circuit being connected with the empty liquid normal pressure wing passage of plate type heat exchanger (20), and make The empty liquid normal pressure wing passage of plate type heat exchanger (20) is disconnected with the closed circuit of corresponding connection, makes the sky of plate type heat exchanger (20) Liquid normal pressure wing passage is connected with air and keeps nothing liquid status;Or, open the circulation being connected with empty liquid normal pressure wing passage Air bleeding valve on loop, closes other valves that the empty liquid normal pressure wing passage of plate type heat exchanger (20) is connected with tank case (1), makes The empty liquid normal pressure wing passage of plate type heat exchanger (20) is connected with air by air bleeding valve and keeps nothing liquid status;
The flow signal of the flowmeter on closed circuit that S2, collection are connected with flowing wing passage, adjusts this and loops back Frequency conversion pump power on road, after the working medium flow in this closed circuit is stable, will according to plate type heat exchanger one side channel capacity Ask, change the regulation on this closed circuit according to the flow signal of the flowmeter on the closed circuit being connected with flowing wing passage Valve opening, to meet the side operating mode traffic requirement;
After S3, operating condition of test are stable, the plate that four pressure transmitter measurements are obtained is recorded by plc data acquisition controller Formula exchanger heat side-entrance pressure Phi, plate type heat exchanger hot side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, Plate type heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger drooping characteristic is respectively by pressure Phi, pressure Pho, pressure Pci, pressure Power Pco is calculated.
The beneficial effects of the present invention is:
1) test system in the present invention is required only for the pressure fall-off test of plate type heat exchanger liquid phase medium and is set up, structure phase To simple, it is only necessary to tank case at is configured, without additional configuration temperature control system, unnecessary throwing is greatlyd save Money.
2) test system in the present invention, first circulation feed liquor test pipeline section and second circulation feed liquor are tested the pipe of pipeline section Crossing footpath and length of pipe correspondent equal, first circulation goes out liquid test pipeline section and second circulation goes out the line portals that liquid tests pipeline section Also pipeline bore of the closed circuit of correspondent equal, i.e., two in corresponding position is consistent for footpath and length of pipe, pipe in line one Cause;This test system simultaneously makes the portions such as pressure transmitter in two closed circuits, flowmeter, regulating valve, switch valve and variable frequency pump Part type selecting is consistent, and the installation site of the corresponding part in two closed circuits is consistent.So as to when operating personnel use this survey When test system carries out plate type heat exchanger liquid phase medium pressure fall-off test, working medium is from the outflow of same place tank case, tube side and on-way resistance one Cause, it is ensured that the working medium physical property in two wing passage of plate type heat exchanger is consistent, and avoids hydrostatic head pressure difference to test result Impact.
3) Flow-rate adjustment module and pressure balance module are provided with the present invention, it is ensured that plate type heat exchanger is warm, cold both sides The flow of passage, inlet pressure are controlled, and ensure that the realizability of three kinds of testing schemes.In two wing passage work of plate type heat exchanger In the one wing passage flowing of matter uniform flow testing scheme and plate type heat exchanger, another wing passage topping up equipressure testing scheme, by In the uniformity of two closed circuit tube sides, and under the control of plc data acquisition controller two variable frequency pump actions same Step property, working medium simultaneously enters hot, cold two wing passages of plate type heat exchanger, and the inlet pressure of two wing passages is same or like, So as to reduce significantly because working medium enter the big caused plate deformation of pressure reduction of two wing passage sequencings and two wing passages because Impact of the element to test result.
From three kinds of different testing schemes that test system matches, plate type heat exchanger liquid phase medium pressure fall-off test result pair is made Operating mode is actual with more directiveness, and the contrast of the test data of three groups of testing schemes also reflects the property of heat exchange plate from side Energy.
Description of the drawings
Fig. 1 is the structural representation of liquid-liquid measurement system of the prior art.
Fig. 2 is the structural representation of the plate type heat exchanger liquid phase medium pressure fall-off test system in the present invention.
The implication of in figure label symbol is as follows:
A- liquid storage vessel b- cooling tower c- cooler d- plate type heat exchanger e- heater
1 gravity tank case, 2/3 stop valve, 4 first variable frequency pump, 5 second variable frequency pump
6/7 check-valves, 8 first flowmeter, 9 second flowmeter
10 first 11 second regulating valve of regulating valve, 12 first switch valve
13 second switch valve, 14 first balanced valve, 15 second balanced valve
16 first test pipeline sections 17 second test 20 plate type heat exchanger of pipeline section
23 the 3rd test pipeline sections 24 the 4th test the 3rd switch valve of pipeline section 25
26 the 4th switch valve, 27 first row air valve, 28 second row air valve
18/19/21/22 pressure transmitter
Specific embodiment
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 carried out clear, complete Site preparation is described, it is clear that described embodiment is only a part of embodiment of the present invention, rather than whole embodiments.It is based on Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under the premise of creative work is not made Embodiment, belongs to the scope of protection of the invention.
As shown in Fig. 2 a kind of plate type heat exchanger liquid phase medium pressure fall-off test system, including tank case 1 and plate type heat exchanger 20, It is provided with connection first circulation feed liquor test pipeline section 16, first circulation each other to go out between the tank case 1 and plate type heat exchanger 20 Liquid test pipeline section 23 and second circulation feed liquor test pipeline section 17, second circulation go out liquid test pipeline section 24, and the first circulation is entered Liquid test pipeline section 16, first circulation goes out liquid test pipeline section 23 and constitutes first circulation loop, and the second circulation feed liquor tests pipeline section 17th, second circulation goes out the liquid test composition of pipeline section 24 second circulation loop.
It is pointed out that first circulation loop and second circulation loop can selectively with plate type heat exchanger hot side Passage or cold side channel are connected, i.e., first circulation loop can be with appointing in the hot-side channel of plate type heat exchanger or cold side channel One passage of meaning is connected, and second circulation loop is then connected with another passage.
As shown in Fig. 2 being respectively provided with the first circulation feed liquor test pipeline section 16 and second circulation feed liquor test pipeline section 17 There are working medium conveyor module and Flow-rate adjustment module;The working medium conveyor module is for being arranged on first circulation feed liquor test pipeline section 16 The first variable frequency pump 4 and be arranged on second circulation feed liquor test pipeline section 17 on the second variable frequency pump 5.The Flow-rate adjustment module For the first flowmeter 8 that arranges to 20 order of plate type heat exchanger from tank case 1 being arranged on first circulation feed liquor test pipeline section 16 With the first regulating valve 10, and for be arranged on second circulation feed liquor test pipeline section 17 on suitable to plate type heat exchanger 20 from tank case 1 The second flowmeter 9 and the second regulating valve 11 of sequence arrangement;First variable frequency pump 4 is arranged between tank case 1 and first flowmeter 8 First circulation feed liquor test pipeline section 16 on, second variable frequency pump 5 is arranged between tank case 1 and second flowmeter 9 second On circulation feed liquor test pipeline section 17.
As shown in Fig. 2 the first circulation feed liquor test pipeline section 16, first circulation goes out liquid test pipeline section 23, second circulation Feed liquor test pipeline section 17, second circulation goes out liquid test pipeline section 24 and is provided with pressure measxurement mould with the junction of plate type heat exchanger 20 Block;The pressure measuring module is respectively the pressure transmitter 18 according to position as shown in Figure 2 installation, pressure transmitter 19, pressure Power transmitter 21 and pressure transmitter 22.
This test system is also arranged on the respective at least one test pipeline section in first circulation loop and second circulation loop There is exhaust module.The exhaust module is to be arranged on the first row air valve 27, Yi Jishe that first circulation goes out on liquid test pipeline section 23 The second row air valve 28 gone out on liquid test pipeline section 24 in second circulation is put, the first row air valve 27 goes out liquid test in first circulation The installation site correspondence that pipeline section 23 goes out on liquid test pipeline section 24 in second circulation with second row air valve 28 is identical.Certainly, first row Air valve 27 and second row air valve 28 should be arranged on a high position for corresponding test pipeline section or high point, in order to exclude gas.
The caliber and length of pipe of the first circulation feed liquor test pipeline section 16 and second circulation feed liquor test pipeline section 17 Correspondent equal, first circulation go out caliber and the length of pipe correspondence that liquid test pipeline section 23, second circulation goes out liquid test pipeline section 24 Equal;Working medium conveyor module and Flow-rate adjustment module test pipeline section 16 in first circulation feed liquor and second circulation feed liquor tests pipeline section Installation site correspondence on 17 is identical, and the model correspondence of corresponding component is identical.First variable frequency pump 4 and the second variable frequency pump 5, first-class Gauge 8 and second flowmeter 9, the first regulating valve 10 and the second regulating valve 11, pressure transmitter 18 and pressure transmitter 19, pressure Transmitter 21 and pressure transmitter 22, first row air valve 27 and second row air valve 28 one group and are corresponded to each other two-by-two, each group Number of element types and the installation site all same in corresponding pipeline are consistent, all parts all with plc data acquisition controller phase Connection.
As shown in Fig. 2 this test system also includes pressure balance module, the pressure balance module includes that connecting first follows Ring feed liquor test pipeline section 16 and second circulation feed liquor test the pressure-equalizing pipe of pipeline section 17, the pressure-equalizing pipe and first circulation The pressure transmitter 18 and first that the junction of feed liquor test pipeline section 16 is arranged on first circulation feed liquor test pipeline section 16 is adjusted Between valve 10, the pressure-equalizing pipe is arranged on the test of second circulation feed liquor with the junction of second circulation feed liquor test pipeline section 17 Between pressure transmitter 19 on pipeline section 17 and the second regulating valve 11;The pressure-equalizing pipe is near the test of first circulation feed liquor The first balanced valve 14 is provided with the pipe shaft of pipeline section 16, and the pressure-equalizing pipe is near second circulation feed liquor test pipeline section 17 The second balanced valve 15 is provided with pipe shaft.
Three kinds of testing schemes to test system in the present invention are described in detail below in conjunction with the accompanying drawings.
Embodiment 1
In this testing scheme, plate type heat exchanger 20 be respectively connected with logical two with first circulation loop and second circulation loop Working medium in individual passage (i.e. hot-side channel in plate type heat exchanger and cold side channel) is flowed for uniform flow, and this method of testing includes Following steps:
S1, is first turned on stop valve 2, stop valve 3, opens first switch valve 12, second switch valve 13, the 3rd switch valve 25th, the 4th switch valve 26, the first variable frequency pump of low-frequency start 4, the second variable frequency pump 5, standard-sized sheet the first regulating valve 10, the second regulating valve 11, first row air valve 27, second row air valve 28 is then turned on, wait draining in pipe-line system after fixed gas, closes first row air valve 27th, second row air valve 28;Now the first balanced valve 14 and the second balanced valve 15 are all remained off;
The flow signal of S2, collection first flowmeter 8 and second flowmeter 9, adjusts the first variable frequency pump 4, the second variable frequency pump 5 Power, after the stability of flow in two circulation lines, requires according to plate type heat exchanger both sides channel capacity, according to first flow Count 8 flow signals and change 10 aperture of the first regulating valve, change 11 aperture of the second regulating valve according to 9 flow signal of second flowmeter, To meet the operating mode traffic requirement in two closed circuits;
After S3, operating condition of test are stable, by plc data acquisition controller record pressure transmitter 18, pressure transmitter 19, Pressure transmitter 21 and pressure transmitter 22 measure plate type heat exchanger hot side import pressure Phi, the plate type heat exchanger heat for obtaining Side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, plate type heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger Drooping characteristic is calculated by pressure Phi, pressure Pho, pressure Pci, pressure Pco respectively, and this calculating process belongs to common knowledge, Will not be described in detail herein.
It should be noted that:In the step of this testing scheme S1, S2, first variable frequency pump 4 and the second variable frequency pump 5 Flow-rate adjustment in startup and two closed circuits synchronously will be carried out.
Embodiment 2
In this testing scheme, the work that passage that plate type heat exchanger 20 is connected with first circulation loop is flowed in wing passage Matter is in flow regime, is full of work with second circulation loop in the passage that plate type heat exchanger 20 is connected i.e. topping up pressurize wing passage Matter and working medium does not flow, the flowing wing passage of plate type heat exchanger 20 are identical with the working medium hydraulic pressure in topping up pressurize wing passage;
This method of testing comprises the steps:
S1, stop valve 2 is opened, open first switch valve 12, the 3rd switch valve 25, the first regulating valve of standard-sized sheet 10, open One balanced valve 14 and the second balanced valve 15, make the flowing wing passage in plate type heat exchanger 20 be connected with topping up pressurize wing passage; The first variable frequency pump of low-frequency start 4, then turns on first row air valve 27, wait draining in pipe-line system after fixed gas, closes air bleeding valve 27;In the process, the stop valve 3 on second circulation loop, second switch valve 13, the 4th switch valve 26 is made to remain turned-off shape State;
The flow signal of the first flowmeter 8 on S2, collection first circulation loop, adjusts 4 power of the first variable frequency pump, treats the After working medium flow in one closed circuit is stablized, required according to plate type heat exchanger one side channel capacity, according to first flowmeter 8 Flow signal changes 10 aperture of the first regulating valve, to meet the operating mode traffic requirement of flowing wing passage;
After S3, operating condition of test are stable, by plc data acquisition controller record pressure transmitter 18, pressure transmitter 19, Pressure transmitter 21 and pressure transmitter 22 measure plate type heat exchanger hot side import pressure Phi, the plate type heat exchanger heat for obtaining Side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, plate type heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger Drooping characteristic is calculated by pressure Phi, pressure Pho, pressure Pci, pressure Pco respectively.
Embodiment 3
In this testing scheme, the work that passage that plate type heat exchanger 20 is connected with first circulation loop is flowed in wing passage Matter is in flow regime, the passage that plate type heat exchanger 20 is connected with second circulation loop i.e. sky liquid normal pressure wing passage and big gas phase Logical;This method of testing comprises the steps:
S1, the stop valve 2 that opens in first circulation loop, open first switch valve 12, the 3rd switch valve 25, standard-sized sheet first Regulating valve 10, the first variable frequency pump of low-frequency start 4, first row air valve 27 is then turned on, wait draining in pipe-line system after fixed gas, is closed Close first row air valve 27;In the process, stop valve 3 on second circulation loop, second switch valve 13, the 4th switch valve 26 are made Remain off, and so that plate type heat exchanger 20 is mutually disconnected with second circulation loop, now the empty liquid normal pressure of plate type heat exchanger 20 Passage is directly communicated with air;Meanwhile, so that the first balanced valve 14 and the second balanced valve 15 is also remained off.
If it should be noted that the installation site of second row air valve 28 is just in second switch valve 13 and the 4th switch valve On second circulation loop between 26, then second row air valve 28 can also be opened, make the empty liquid normal pressure of now plate type heat exchanger 20 Passage is directly communicated with air;
S2, the flow signal of collection first flowmeter 8, adjust 4 power of the first variable frequency pump, treat the stream in first circulation loop After amount is stable, is required according to plate type heat exchanger one side channel capacity, change the first regulating valve according to 8 flow signal of first flowmeter 10 apertures, to meet the operating mode traffic requirement of flowing wing passage.
After S3, operating condition of test are stable, by plc data acquisition controller record pressure transmitter 18, pressure transmitter 19, Pressure transmitter 21 and pressure transmitter 22 measure plate type heat exchanger hot side import pressure Phi, the plate type heat exchanger heat for obtaining Side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, plate type heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger Drooping characteristic is calculated by pressure Phi, pressure Pho, pressure Pci, pressure Pco respectively.

Claims (10)

1. a kind of plate type heat exchanger liquid phase medium pressure fall-off test system, it is characterised in that:Including tank case (1) and plate type heat exchanger (20), be provided between described tank case (1) and plate type heat exchanger (20) connection each other first circulation feed liquor test pipeline section (16), First circulation goes out liquid test pipeline section (23) and second circulation feed liquor test pipeline section (17), second circulation go out liquid test pipeline section (24), first circulation feed liquor test pipeline section (16), first circulation go out liquid test pipeline section (23) composition first circulation loop, institute State second circulation feed liquor test pipeline section (17), second circulation and go out liquid test pipeline section (24) composition second circulation loop;
Working medium conveying is provided with first circulation feed liquor test pipeline section (16) and second circulation feed liquor test pipeline section (17) Module and Flow-rate adjustment module;
First circulation feed liquor test pipeline section (16), first circulation go out liquid test pipeline section (23), second circulation feed liquor testing tube Section (17), second circulation go out liquid test pipeline section (24) and are provided with pressure measuring module with the junction of plate type heat exchanger (20);
This test system row of being provided with also on the respective at least one test pipeline section in first circulation loop and second circulation loop Gas module.
2. plate type heat exchanger liquid phase medium pressure fall-off test system as claimed in claim 1, it is characterised in that:The first circulation The caliber and length of pipe correspondent equal of feed liquor test pipeline section (16) and second circulation feed liquor test pipeline section (17), first circulation Go out caliber and length of pipe correspondent equal that liquid test pipeline section (23), second circulation go out liquid test pipeline section (24);Working medium is conveyed The peace of module and Flow-rate adjustment module on first circulation feed liquor test pipeline section (16) and second circulation feed liquor test pipeline section (17) Holding position correspondence is identical, and the model correspondence of corresponding component is identical.
3. plate type heat exchanger liquid phase medium pressure fall-off test system as claimed in claim 1 or 2, it is characterised in that:The working medium Conveyor module for the first variable frequency pump (4) for being arranged on first circulation feed liquor test pipeline section (16) and is arranged on second circulation and enters The second variable frequency pump (5) on liquid test pipeline section (17).
4. plate type heat exchanger liquid phase medium pressure fall-off test system as claimed in claim 3, it is characterised in that:The Flow-rate adjustment Module for be arranged on first circulation feed liquor test pipeline section (16) from tank case (1) to plate type heat exchanger (20) order arrangement the Flow meters (8) and the first regulating valve (10), and for be arranged on second circulation feed liquor test pipeline section (17) from tank case (1) Second flowmeter (9) and the second regulating valve (11) to plate type heat exchanger (20) order arrangement;Described first variable frequency pump (4) are arranged On first circulation feed liquor test pipeline section (16) between tank case (1) and first flowmeter (8), the second variable frequency pump (5) set Put on second circulation feed liquor test pipeline section (17) between tank case (1) and second flowmeter (9).
5. plate type heat exchanger liquid phase medium pressure fall-off test system as claimed in claim 1, it is characterised in that:The pressure measxurement Module is pressure transmitter.
6. plate type heat exchanger liquid phase medium pressure fall-off test system as claimed in claim 1, it is characterised in that:The exhaust module Go out, for being arranged on first circulation, the first row air valve (27) that liquid is tested on pipeline section (23), and be arranged on second circulation and go out liquid test Second row air valve (28) on pipeline section (24), first row air valve (27) go out liquid test pipeline section (23) and second in first circulation The installation site that air bleeding valve (28) goes out on liquid test pipeline section (24) in second circulation corresponds to identical.
7. plate type heat exchanger liquid phase medium pressure fall-off test system as claimed in claim 4, it is characterised in that:This test system is also Including pressure balance module, the pressure balance module includes that connecting first circulation feed liquor test pipeline section (16) and second circulation enters The pressure-equalizing pipe of liquid test pipeline section (17), the pressure-equalizing pipe are set with the junction of first circulation feed liquor test pipeline section (16) Put between the pressure measuring module on first circulation feed liquor test pipeline section (16) and the first regulating valve (10), the pressure balance Pipe is arranged on the pressure on second circulation feed liquor test pipeline section (17) with the junction of second circulation feed liquor test pipeline section (17) and surveys Between amount module and the second regulating valve (11);The pressure-equalizing pipe is in the pipe shaft near first circulation feed liquor test pipeline section (16) On be provided with the first balanced valve (14), the pressure-equalizing pipe is set on the pipe shaft near second circulation feed liquor test pipeline section (17) It is equipped with the second balanced valve (15).
8. a kind of method of testing of the plate type heat exchanger liquid phase medium pressure fall-off test system using as shown in claim 4, which is special Levy be plate type heat exchanger (20) be respectively connected with the work in logical two passage with first circulation loop and second circulation loop Matter is flowed for uniform flow, and this method of testing comprises the steps:
S1, the cutting-off valve being first turned on first circulation loop and second circulation loop, start the first variable frequency pump (4) and second Variable frequency pump (5), the first regulating valve of standard-sized sheet (10) and the second regulating valve (11), open first row air valve (27), second row air valve (28), after the fixed gas in pipeline is drained, first row air valve (27), second row air valve (28) are closed;
The flow signal of S2, collection first flowmeter (8) and second flowmeter (9), adjusts the first variable frequency pump (4), the second frequency conversion Pump (5) power, after stability of flow in pipeline, requires according to plate type heat exchanger both sides channel capacity, according to first flowmeter (8) Flow signal changes the first regulating valve (10) aperture, changes the second regulating valve (11) according to second flowmeter (9) flow signal and opens Degree, to meet the operating mode traffic requirement in two closed circuits;
After S3, operating condition of test are stable, record that four pressure transmitter measurements obtain by plc data acquisition controller board-like changes Hot device hot side import pressure Phi, plate type heat exchanger hot side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, board-like Heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger drooping characteristic is respectively by pressure Phi, pressure Pho, pressure Pci, pressure Pco Calculate;
Flow-rate adjustment in step S1, S2, in the startup of the first variable frequency pump (4) and the second variable frequency pump (5) and two closed circuits Synchronously to carry out.
9. a kind of method of testing of the plate type heat exchanger liquid phase medium pressure fall-off test system using as shown in claim 4, which is special Levy the work for being that the passage that plate type heat exchanger (20) is connected with a loop in two closed circuits is flowed in wing passage Matter is in flow regime, is full of work with another loop in the passage that plate type heat exchanger (20) is connected i.e. topping up pressurize wing passage Matter and working medium does not flow, the flowing wing passage of plate type heat exchanger (20) are identical with the working medium hydraulic pressure in topping up pressurize wing passage;
This method of testing is provided with pressure balance module in a test system, and the pressure balance module includes to connect first circulation Feed liquor test pipeline section (16) and the pressure-equalizing pipe of second circulation feed liquor test pipeline section (17), the pressure-equalizing pipe are followed with first The junction of ring feed liquor test pipeline section (16) is arranged on the pressure measuring module on first circulation feed liquor test pipeline section (16) and the Between one regulating valve (10), the pressure-equalizing pipe is arranged on second with the junction of second circulation feed liquor test pipeline section (17) and follows Between pressure measuring module and the second regulating valve (11) on ring feed liquor test pipeline section (17);The pressure-equalizing pipe is near the The first balanced valve (14) is provided with the pipe shaft of one circulation feed liquor test pipeline section (16), the pressure-equalizing pipe is being followed near second The second balanced valve (15) is provided with the pipe shaft of ring feed liquor test pipeline section (17).
This method of testing comprises the steps:
S1, the cutting-off valve that opens on the closed circuit being connected with flowing wing passage, make to be connected with topping up pressurize wing passage Closed circuit on cutting-off valve remain off, standard-sized sheet and the regulation on the flowing closed circuit that is connected of wing passage Valve, opens the first balanced valve (14) and the second balanced valve (15), so that the flowing wing passage in plate type heat exchanger (20) is protected with topping up Pressure wing passage is connected;Start the variable frequency pump on the closed circuit being connected with flowing wing passage, open on this closed circuit Air bleeding valve, after the fixed gas in this closed circuit is drained, the air bleeding valve closed on this closed circuit;
The flow signal of the flowmeter on closed circuit that S2, collection are connected with flowing wing passage, is adjusted on this closed circuit Frequency conversion pump power, after the working medium flow in this closed circuit is stable, required according to plate type heat exchanger one side channel capacity, according to Change the regulating valve on this closed circuit according to the flow signal of the flowmeter on the closed circuit being connected with flowing wing passage to open Degree, to meet the side operating mode traffic requirement;
After S3, operating condition of test are stable, record that four pressure transmitter measurements obtain by plc data acquisition controller board-like changes Hot device hot side import pressure Phi, plate type heat exchanger hot side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, board-like Heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger drooping characteristic is respectively by pressure Phi, pressure Pho, pressure Pci, pressure Pco Calculate.
10. a kind of method of testing of the plate type heat exchanger liquid phase medium pressure fall-off test system using as shown in claim 4, which is special Levy the work for being that the passage that plate type heat exchanger (20) is connected with a loop in two closed circuits is flowed in wing passage Matter is in flow regime, and another passage of plate type heat exchanger (20) is that empty liquid normal pressure wing passage is communicated with air;This test side Method comprises the steps:
S1, the cutting-off valve that opens on the closed circuit being connected with flowing wing passage, standard-sized sheet are connected with flowing wing passage Regulating valve on closed circuit;Start the variable frequency pump on the closed circuit being connected with flowing wing passage, open this closed circuit On air bleeding valve, after the fixed gas in this closed circuit is drained, the air bleeding valve closed on this closed circuit;
The cutting-off valve that closes on the closed circuit being connected with the empty liquid normal pressure wing passage of plate type heat exchanger (20), and make board-like The empty liquid normal pressure wing passage of heat exchanger (20) is disconnected with the closed circuit of corresponding connection, makes the empty liquid of plate type heat exchanger (20) normal Pressure wing passage is connected with air and keeps nothing liquid status;Or, open the closed circuit being connected with empty liquid normal pressure wing passage On air bleeding valve, close other valves for being connected with tank case (1) of empty liquid normal pressure wing passage of plate type heat exchanger (20), make board-like The empty liquid normal pressure wing passage of heat exchanger (20) is connected with air by air bleeding valve and keeps nothing liquid status;
The flow signal of the flowmeter on closed circuit that S2, collection are connected with flowing wing passage, is adjusted on this closed circuit Frequency conversion pump power, after the working medium flow in this closed circuit is stable, required according to plate type heat exchanger one side channel capacity, according to Change the regulating valve on this closed circuit according to the flow signal of the flowmeter on the closed circuit being connected with flowing wing passage to open Degree, to meet the side operating mode traffic requirement;
After S3, operating condition of test are stable, record that four pressure transmitter measurements obtain by plc data acquisition controller board-like changes Hot device hot side import pressure Phi, plate type heat exchanger hot side outlet pressure Pho, plate type heat exchanger cold side import pressure Pci, board-like Heat exchanger cold side outlet port pressure Pco;Plate type heat exchanger drooping characteristic is respectively by pressure Phi, pressure Pho, pressure Pci, pressure Pco Calculate.
CN201611029975.2A 2016-11-15 2016-11-15 Plate heat exchanger liquid phase medium pressure fall-off test system and its test method Active CN106482973B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611029975.2A CN106482973B (en) 2016-11-15 2016-11-15 Plate heat exchanger liquid phase medium pressure fall-off test system and its test method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611029975.2A CN106482973B (en) 2016-11-15 2016-11-15 Plate heat exchanger liquid phase medium pressure fall-off test system and its test method

Publications (2)

Publication Number Publication Date
CN106482973A true CN106482973A (en) 2017-03-08
CN106482973B CN106482973B (en) 2018-12-04

Family

ID=58274106

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611029975.2A Active CN106482973B (en) 2016-11-15 2016-11-15 Plate heat exchanger liquid phase medium pressure fall-off test system and its test method

Country Status (1)

Country Link
CN (1) CN106482973B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107238627A (en) * 2017-05-31 2017-10-10 中国科学院上海应用物理研究所 Conduction oil working medium forced circulation Comprehensive Experiment circuit system
CN107702581A (en) * 2017-10-31 2018-02-16 中国计量大学 The observation device of biphase gas and liquid flow in the plate type heat exchanger of adjustable mounting position
CN108982090A (en) * 2018-08-13 2018-12-11 江苏大学镇江流体工程装备技术研究院 A kind of pressure loss test macro and its test method
CN110423655A (en) * 2019-08-09 2019-11-08 合肥欧力杰工程技术有限公司 A kind of Wort cooling plate heat exchanger device for preventing leakage and its application method
CN111189735A (en) * 2020-01-20 2020-05-22 上海交通大学 Oil-containing refrigerant/stagnant oil testing device and method for plate heat exchanger and single pipe
CN113899569A (en) * 2021-08-17 2022-01-07 合肥通用机械研究院有限公司 Heat exchanger performance and service life testing device and testing method using same

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1306653A1 (en) * 2001-10-29 2003-05-02 Wade W. Smith Water management system
CN102175351A (en) * 2011-03-11 2011-09-07 合肥通用机械研究院 Device for testing thermal performance and fluid resistance of liquid-liquid heat exchanger
CN102200491A (en) * 2010-03-26 2011-09-28 上海瀚艺冷冻机械有限公司 Test bench for water source heat pump
CN203758764U (en) * 2014-03-14 2014-08-06 浙江天煌科技实业有限公司 Heat exchanger integrated comprehensive performance testing system
CN104280258A (en) * 2014-10-14 2015-01-14 洛阳双瑞特种装备有限公司 Comprehensive heat power engineering system used for heat exchanger test

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1306653A1 (en) * 2001-10-29 2003-05-02 Wade W. Smith Water management system
CN102200491A (en) * 2010-03-26 2011-09-28 上海瀚艺冷冻机械有限公司 Test bench for water source heat pump
CN102175351A (en) * 2011-03-11 2011-09-07 合肥通用机械研究院 Device for testing thermal performance and fluid resistance of liquid-liquid heat exchanger
CN203758764U (en) * 2014-03-14 2014-08-06 浙江天煌科技实业有限公司 Heat exchanger integrated comprehensive performance testing system
CN104280258A (en) * 2014-10-14 2015-01-14 洛阳双瑞特种装备有限公司 Comprehensive heat power engineering system used for heat exchanger test

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
付小平: "《空调技术》", 28 February 2011 *
俞立凡 等: "板式换热器换热板片微变形特性浅析", 《华电技术》 *
张海泉: "板式换热器热工与阻力性能测试及计算方法研究", 《中国优秀博硕士学位论文全文数据库(硕士)工程科技Ⅱ辑》 *
徐志明 等: "板式换热器传热和阻力特性的实验研究", 《热科学与及技术》 *

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107238627A (en) * 2017-05-31 2017-10-10 中国科学院上海应用物理研究所 Conduction oil working medium forced circulation Comprehensive Experiment circuit system
CN107238627B (en) * 2017-05-31 2020-03-27 中国科学院上海应用物理研究所 Comprehensive experiment loop system for forced circulation of heat conduction oil working medium
CN107702581A (en) * 2017-10-31 2018-02-16 中国计量大学 The observation device of biphase gas and liquid flow in the plate type heat exchanger of adjustable mounting position
CN107702581B (en) * 2017-10-31 2019-05-03 中国计量大学 The observation device of biphase gas and liquid flow in the plate heat exchanger of adjustable mounting position
CN108982090A (en) * 2018-08-13 2018-12-11 江苏大学镇江流体工程装备技术研究院 A kind of pressure loss test macro and its test method
CN110423655A (en) * 2019-08-09 2019-11-08 合肥欧力杰工程技术有限公司 A kind of Wort cooling plate heat exchanger device for preventing leakage and its application method
CN110423655B (en) * 2019-08-09 2024-02-27 合肥欧力杰智能装备系统有限公司 Leakage-proof device of wort cooling plate type heat exchanger and use method thereof
CN111189735A (en) * 2020-01-20 2020-05-22 上海交通大学 Oil-containing refrigerant/stagnant oil testing device and method for plate heat exchanger and single pipe
CN113899569A (en) * 2021-08-17 2022-01-07 合肥通用机械研究院有限公司 Heat exchanger performance and service life testing device and testing method using same
CN113899569B (en) * 2021-08-17 2023-10-03 合肥通用机械研究院有限公司 Heat exchanger performance and service life testing device and testing method using same

Also Published As

Publication number Publication date
CN106482973B (en) 2018-12-04

Similar Documents

Publication Publication Date Title
CN106482973A (en) Plate type heat exchanger liquid phase medium pressure fall-off test system and its method of testing
CN106441797B (en) The automatic flow resistance test macro of cold plate
CN201289435Y (en) Test stand for heat dispersion of radiator
CN103983464B (en) Heat exchanger performance test platform
CN103592142A (en) System for testing heat transfer and resistance characteristics of large-size generating equipment heat exchanger
CN109945943B (en) Bidirectional flow resistance testing system and method suitable for different fluid devices
CN104280258A (en) Comprehensive heat power engineering system used for heat exchanger test
CN108955081A (en) Cooling system
CN102175351B (en) Device for testing thermal performance and fluid resistance of liquid-liquid heat exchanger
CN203479550U (en) System suitable for testing heat transfer and resistance characteristics of heat exchanger of large-scale generating equipment
CN105222230A (en) Inter-row air conditioner, pressure regulating method of inter-row air conditioner and inter-row air conditioning system
CN203465038U (en) Large-caliber-calorimeter calibrating device
CN116006358B (en) Cold helium pressurization ground test system and method
CN105973506A (en) Cold-hot independent circulation calorimeter durability test device
CN206725241U (en) A kind of large-scale water-hydrothermal exchange equipment test device
CN207366057U (en) It is a kind of can simulation medium actual use temperature gas flowmeter standard set-up
CN202693298U (en) Performance detection test stand of airplane environment control accessory
CN109855900A (en) A kind of climbing-falling film evaporator integration test experimental system
CN202008414U (en) Testing device for thermal performance and fluid resistance of liquid-liquid heat exchanger
CN214748332U (en) Novel gas flow verification device for loop
CN214224545U (en) High-temperature working state test system for fuel test piece
CN107727166B (en) A kind of automobile power cell packet internal cooling system fluid flow test method
CN105136342A (en) System and method for improving measurement precision of heat exchange amount of heat exchanger under temperature differential condition
CN113851674A (en) Thermal management system for testing fuel cell system
CN209542123U (en) A kind of climbing-falling film evaporator simulation test system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
CB02 Change of applicant information
CB02 Change of applicant information

Address after: 230031 No. 888 Changjiang West Road, Shushan District, Hefei, Anhui.

Applicant after: Hefei General Machinery Research Institute Co., Ltd.

Applicant after: Gansu boiler pressure vessel inspection Inst

Address before: 230031 No. 888 Changjiang West Road, Shushan District, Hefei, Anhui.

Applicant before: Hefei Universal Machinery Inst.

Applicant before: Gansu boiler pressure vessel inspection Inst

GR01 Patent grant
GR01 Patent grant