CN204556552U - A kind of multi-channel parallel heat release rate testing system - Google Patents
A kind of multi-channel parallel heat release rate testing system Download PDFInfo
- Publication number
- CN204556552U CN204556552U CN201520250732.6U CN201520250732U CN204556552U CN 204556552 U CN204556552 U CN 204556552U CN 201520250732 U CN201520250732 U CN 201520250732U CN 204556552 U CN204556552 U CN 204556552U
- Authority
- CN
- China
- Prior art keywords
- smoke
- flue gas
- sensor
- discharging pipe
- heat release
- 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.)
- Expired - Fee Related
Links
Landscapes
- Sampling And Sample Adjustment (AREA)
Abstract
The utility model discloses a kind of multi-channel parallel heat release rate testing system, aim to provide a kind of mode using multi-channel parallel, the fire that, HRR large to burning area is high carries out the system of accurate calorimetric.Comprise firing chamber, data acquisition unit, data processor and multiple test cell; Each test cell comprises gas collection system, flue gas flow measuring system and flue gas sampling system, and gas collection system comprises smoke discharging pipe, honeycomb screen, sampling section and smoke exhaust fan; Flue gas flow measuring system comprises two-way pitot tube, differential pressure pick-up and thermopair; Flue gas sampling system comprises flue gas sampling pipe, condenser, smoke filter, drying device, sampling pump, spinner-type flowmeter, lambda sensor, CO
2sensor, CO sensor; Smoke discharging pipe in each test cell is connected in parallel.The utility model can be applicable to the heat release rate testing of tunnel fire hazard, also can be used for the test of the HRR to automobile, train fire.
Description
Technical field
The utility model relates to a kind of heat release rate testing system, in particular, relates to a kind of multi-channel parallel heat release rate testing system measuring high-power heat release rate.
Background technology
The heat discharged in unit interval when HRR is combustible combustion.All the time, HRR is all regarded as the most important parameter reflecting fire scenario, sign fire process.By multi-form experiment, people have developed the method for multiple measurement HRR, and at present by everybody well accepted measuring method mainly weight-loss method and oxygen consumption method, and oxygen consumption method is the main stream approach of carrying out fire research.
Oxygen consumption method refers to, net heat of combustion and the oxygen quality that consumes of burning are ratio, and this relation often consumes the heat that 1kg oxygen discharges to be approximately 13.10 × 10
3kJ is exactly that profit calculates combustible energy discharged in combustion in this way in actual applications.
At present, the range of existing HRR measurement mechanism is all fixed value substantially, when heat release rate size variation is larger, is difficult to meet the requirement of measurement result to range and precision simultaneously.Therefore be necessary the heat release rate testing system studying a kind of multi-channel parallel, when studied fire scale is less, adopts wall scroll smoke-exhaust pipeline to carry out fume collection, thus meet the requirement of system to precision; When fire source power is larger, adopts the method for many smoke-exhaust pipeline parallel connections to carry out fume collection, thus meet the requirement of system to range.
At present, substantially be all for the less comburant of area for carrying out HRR research institute designed system, when comburant area is larger, the flue gas scope produced is larger, and the flue gas flow that single smoke exhaust fan can discharge is limited, and wall scroll smoke discharging pipe is subject to the restriction of space and size, flue gas can not be collected completely by smoke discharging pipe, and measurement result can be made inaccurate.
Utility model content
The purpose of this utility model is the technological deficiency for existing in prior art, and a kind of range and the precision that can improve heat release rate testing are provided, different occasion can be applied in, in real time, accurately can reflect the multi-channel parallel heat release rate testing system of HRR situation of change in combustion process.
The technical scheme adopted for realizing the purpose of this utility model is:
A kind of multi-channel parallel heat release rate testing system, comprises firing chamber, data acquisition unit, data processor and multiple test cell; Each described test cell comprises gas collection system, flue gas flow measuring system and flue gas sampling system, and described gas collection system comprises smoke discharging pipe, honeycomb screen, sampling section and smoke exhaust fan; Described flue gas flow measuring system comprises two-way pitot tube, differential pressure pick-up and thermopair; Described flue gas sampling system comprises flue gas sampling pipe, condenser, smoke filter, drying device, sampling pump, spinner-type flowmeter, lambda sensor, CO
2sensor, CO sensor; Described smoke discharging pipe is respectively by exhaust opening and described combustion chamber, and the described smoke discharging pipe in each described test cell is connected in parallel; Described sampling section is arranged at the described well-mixed position of smoke discharging pipe inside smoke, and it is inner that described honeycomb screen is installed on described smoke discharging pipe, and described smoke exhaust fan is installed on the endpiece of described smoke discharging pipe; Be provided with described two-way pitot tube, thermopair and flue gas sampling pipe in described sampling section, described two-way pitot tube is connected with described differential pressure pick-up; The flue gas output terminal of described flue gas sampling pipe successively with described condenser, smoke filter, drying device, sampling pump, spinner-type flowmeter, lambda sensor, CO
2sensor is connected with CO sensor, described thermopair, differential pressure pick-up, lambda sensor, CO
2sensor is connected with the signal input part of described data acquisition unit respectively with the signal output part of CO sensor, and the signal output part of described data acquisition unit is connected with the signal input part of described data processor.
Described exhaust opening is positioned at the sidewall of described firing chamber, and the smoke discharging pipe of each described test cell be arranged in parallel with described firing chamber respectively.
Described burner ends is separately installed with smoke-proof pendant wall.
Described exhaust opening is positioned at the top of described firing chamber, and the smoke discharging pipe of each described test cell is respectively by described exhaust opening and described combustion chamber.
Described burner ends is separately installed with smoke-proof pendant wall.
Described two-way pitot tube is installed on the center line of described smoke discharging pipe.
Described lambda sensor adopts zirconia sensor, and the probe segment of described zirconia sensor is installed in metallic test chamber, and described zirconia sensor is with heating element, and described heating element is connected with direct supply.
Be provided with three-way connection between described sampling pump and spinner-type flowmeter, the arm of described three-way connection is communicated with external environment condition; Described smoke exhaust fan is connected with frequency converter.
Compared with prior art, the beneficial effects of the utility model are:
1., in multi-channel parallel heat release rate testing system of the present utility model, measure flow, the concentration of oxygen, the CO of flue gas in smoke-exhaust pipeline respectively with instrument
2concentration, CO concentration, will these data substitute into HRR oxygen consumption method computing formula in can calculate measured by each branch road HRR change, then by the HRR of each branch road be added can obtain comburant HRR change.
2. multi-channel parallel heat release rate testing system of the present utility model adopts the mode of many smoke-exhaust pipeline parallel connections to collect flue gas, increase the total flow of the flue gas that can collect, and the load of every bar smoke-exhaust pipeline and each blower fan can be reduced, reduce the requirement of experiment to equipment.
3. the blower fan of the smoke-exhaust pipeline of multi-channel parallel heat release rate testing system of the present utility model adopts frequency-changing control system, and frequency, by Frequency Converter Control, carries out calculating according to exhaust air rate and determines.
4., in multi-channel parallel heat release rate testing system of the present utility model, measure sampling section and must be arranged on the well-mixed position of flue gas in smoke-exhaust pipeline, namely smoke-exhaust pipeline length of straigh line is at least more than 8 times of diameter.
5., in multi-channel parallel heat release rate testing system of the present utility model, in smoke-exhaust pipeline, the volumetric flow rate of flue gas utilizes pitot tube and differential pressure pick-up to measure.
6. in multi-channel parallel heat release rate testing system of the present utility model, condenser, smoke filtration and drying device is provided with in smoke sampling and analytic system pipeline, in order to reduce the particle and moisture that contain in flue-gas temperature, removing flue gas, to ensure the requirement of testing tool to sample gas.
7. in multi-channel parallel heat release rate testing system of the present utility model, pressure in smoke sampling and analytic system pipeline is provided by sampling pump, flow is regulated by spinner-type flowmeter, connect a three-way connection between sampling pump and spinner-type flowmeter, the arm of three-way connection is used for unnecessary flue gas in discharge line.
8., in multi-channel parallel heat release rate testing system of the present utility model, in smoke sampling and analytic system, each parts are all detachably changed, and use more convenient.
9, multi-channel parallel heat release rate testing system of the present utility model, different according to its structure, go for multiple occasion, the occasions such as such as railway tunnel, vcehicular tunnel, subway tunnel, megastore, station, basement, tunnel rescue station.
Accompanying drawing explanation
Figure 1 shows that the utility model exhaust opening is positioned at the vertical view of sidewall multi-channel parallel heat release rate testing system;
Figure 2 shows that exhaust opening is positioned at the gas collection system sectional drawing of sidewall;
Figure 3 shows that exhaust opening is positioned at the gas collection system schematic diagram of ceiling;
Figure 4 shows that the schematic diagram of lambda sensor;
Figure 5 shows that flue gas flow test macro schematic diagram;
Figure 6 shows that wind speed measuring point distribution schematic diagram in circular row smoke pipeline;
Figure 7 shows that wind speed measuring point distribution schematic diagram in rectangle smoke discharging pipe.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
The schematic diagram of the utility model multi-channel parallel heat release rate testing system as shown in Figure 1, comprises firing chamber 18, data acquisition unit 17, data processor 21 and multiple test cell.; Combustible 2 is placed with in described firing chamber 18.Each described test cell comprises gas collection system, flue gas flow measuring system and flue gas sampling system.Described gas collection system comprises smoke discharging pipe 1, honeycomb screen 23, sampling section 19 and smoke exhaust fan 4; Described flue gas flow measuring system comprises two-way pitot tube 6, differential pressure pick-up 7 and thermopair 22; Described flue gas sampling system comprises flue gas sampling pipe 5, condenser 8, smoke filter 9, drying device 10, sampling pump 11, spinner-type flowmeter 13, lambda sensor 14, CO
2sensor 15, CO sensor 16.Described smoke discharging pipe 1 is communicated with described firing chamber 18 respectively by exhaust opening 3, and the described smoke discharging pipe 1 in each described test cell is connected in parallel.Described sampling section 19 is arranged at the well-mixed position of described smoke discharging pipe 1 inside smoke, and it is inner that described honeycomb screen 23 is installed on described smoke discharging pipe 1, and described smoke exhaust fan 4 is installed on the endpiece of described smoke discharging pipe 1.In order to realize variable frequency control, described smoke exhaust fan 4 is connected with frequency converter 25.Be provided with described two-way pitot tube 6, thermopair 22 and flue gas sampling pipe 5 in described sampling section 19, described two-way pitot tube 6 is connected with described differential pressure pick-up 7.The flue gas output terminal of described flue gas sampling pipe 5 successively with described condenser 8, smoke filter 9, drying device 10, sampling pump 11, spinner-type flowmeter 13, lambda sensor 14, CO
2sensor 15 is connected with CO sensor 16, described thermopair 22, differential pressure pick-up 7, lambda sensor 14, CO
2sensor 15 is connected with the signal input part of described data acquisition unit 17 respectively with the signal output part of CO sensor 16, and the signal output part of described data acquisition unit 17 is connected with the signal input part of described data processor 21.Described two-way pitot tube 6 is installed on the center line of described smoke discharging pipe 1.
Figure 2 shows that exhaust opening is positioned at the gas collection system sectional drawing of sidewall, described exhaust opening 3 is positioned at the sidewall of described firing chamber 18, and the smoke discharging pipe 1 of each described test cell be arranged in parallel with described firing chamber 18 respectively.In the present embodiment, described firing chamber 18 section is rectangular configuration, and two ends, firing chamber 18 are not closed, and install smoke-proof pendant wall at two ends, firing chamber 18 if desired, exhaust opening 3 is positioned on the sidewall of firing chamber 18, and flue gas enters smoke discharging pipe 1 by exhaust opening 3.Honeycomb screen 23 is installed, to make flow of flue gas in smokejack even in smoke discharging pipe 1.Smoke discharging pipe 1 section is rectangle, be arranged in parallel with firing chamber 18.This gas collection system can be applicable to the occasions such as vcehicular tunnel, railway tunnel, subway tunnel, using the runway in tunnel as firing chamber, by the smoke evacuation system in tunnel flue gas collected and measure, thus the HRR of fire in tunnel can be calculated.
Figure 3 shows that exhaust opening is positioned at the gas collection system schematic diagram of ceiling, described exhaust opening 3 is positioned at the top of described firing chamber 18, and the smoke discharging pipe 1 of each described test cell is communicated with described firing chamber 18 respectively by described exhaust opening 3.Two ends, described firing chamber 18 are not closed, and in order to prevent flue gas from overflowing gas collection system, install smoke-proof pendant wall 24 at two ends, firing chamber 18, multiple exhaust openings 3 are positioned at the ceiling of firing chamber 18, and flue gas enters many smoke discharging pipes 1 respectively by exhaust opening 3.Honeycomb screen 23 is installed, to make flow of flue gas in smokejack even in smoke discharging pipe 1.Smoke discharging pipe 1 can be rectangular duct, also can be circular pipe.This gas collection system can be applied to the occasions such as megastore, station, tunnel rescue station, in building, space is as firing chamber, by the smoke evacuation system of building interior setting flue gas collected and measure, thus the HRR of fire in building can be calculated.
Be provided with three-way connection 12 between described sampling pump 11 and spinner-type flowmeter 13, the arm of described three-way connection 12 is communicated with external environment condition, for flue gas unnecessary in discharge line.
Described lambda sensor 14 adopts zirconia sensor, and as shown in Figure 4, the probe segment 26 of described zirconia sensor is installed in metallic test chamber 27 its schematic diagram, and described zirconia sensor is with heating element, and described heating element is connected with direct supply.The change of oxygen concentration in flue gas can be converted into voltage signal by described zirconia sensor, and the output line of sensor is connected with data acquisition unit.
Oxygen concentration is calculated by following formula.
In formula:
oxygen concentration in-flue gas, %;
E-zirconia sensor output potential value, V;
R-ideal gas constant, 8.314J/ (molK);
F-Faraday constant, 96500C/mol;
The absolute temperature of T-zirconia sensor, K;
oxygen concentration in-air, %.
As shown in Figure 5, the physical quantity due to needs measurement is the mean wind speed of section in smoke discharging pipe to the schematic diagram of described smoke discharging pipe flue gas flow test macro, so need to test sectional wind velocity distribution in smoke discharging pipe before use.When described smoke discharging pipe 1 section is circular, as shown in Figure 6, in figure, D is smoke discharging pipe diameter to sectional wind velocity measuring point distribution schematic diagram.。Smoke discharging pipe section is divided into 4 concentric circless, each diameter of a circle relative size as shown in Figure 6, each roundlet be circumferentially evenly distributed 8 measuring points, totally 24 measuring points.When described smoke discharging pipe 1 section is rectangle, as shown in Figure 7, in figure, L is the length of smoke discharging pipe rectangular cross section to sectional wind velocity measuring point distribution schematic diagram, and H is the height of smoke discharging pipe rectangular cross section.During test, open smoke exhaust fan 14, after blower fan running is stable, measure the wind speed at each point position place, then obtain its arithmetic mean, this arithmetic mean is smoke discharging pipe section mean wind speed, is designated as
measure the wind speed v of smoke discharging pipe center position more at the same conditions, v with
ratio be designated as:
Adjustment blower fan frequency, measures the k value change under different wind speed.At the trial, only need to measure wind speed on smoke discharging pipe center line, then be multiplied by k, the mean wind speed of section in smoke discharging pipe can be calculated.Wind speed on described smoke discharging pipe center line uses two-way pitot tube 6 and differential pressure pick-up 7 to measure.Described two-way pitot tube 6 is arranged on smoke discharging pipe center line, and the pressure reduction recorded is converted to electric signal by differential pressure pick-up 7.Gas temperature near two-way pitot tube 6 is by thermocouple measurement, and thermopair should not form disturbance to the air-flow near two-way pitot tube.In smoke discharging pipe, flue gas flow is calculated by following formula.
Wherein:
ρ＝1.29499-0.00455t+1.35716×10
-5t
2-2.99531×10
-8t
3+4.40209×10
-11t
4-3.96413×10
-14t
5+1.95412×10
-17t
6-4.01125×10
-21t
7
In formula: q
vthe volumetric flow rate of flue gas in-smoke discharging pipe, m
3/ s;
A-smoke discharging pipe cross-sectional area, m
2;
Pressure reduction in Δ p-smoke discharging pipe, Pa;
The density of flue gas in ρ-smoke discharging pipe, kg/m
3;
The temperature of flue gas in t-smoke discharging pipe, DEG C.
During use, if test comburant 2 HRR peak value be less than 45% of system range, for satisfied experiment is to the requirement of precision, then uses single channel to measure, only open the smoke exhaust fan 4 of side; If test comburant HRR peak value be more than or equal to 45% of system range, for satisfied experiment is to the requirement of range, then use the measuring method of multi-channel parallel, open the smoke exhaust fan 4 of many sides simultaneously.Before experiment starts, first open smoke exhaust fan 4, after blower fan running is stable, open sampling pump 11, regulate spinner-type flowmeter 13, make the sample airshed flowing through spinner-type flowmeter be 0.5 ~ 2L/min.By lambda sensor 14, CO
2sensor 15, CO sensor 16 access power supply, preheating 5min, then gather the voltage that lambda sensor exports, background potential value when being calculated as lambda sensor by this voltage.After measuring background potential value, keep each instrument continued power, experiment can be started.Light combustible 2, data acquisition unit 17 gathers thermopair 22, differential pressure pick-up 7, lambda sensor 14, CO
2the data of sensor 15, CO sensor 16, data processor 21 can calculate the HRR change measured by each test cell branch road respectively according to these data, then the HRR of each test cell branch road is added the HRR change that can obtain comburant.
HRR is calculated by following formula.
Wherein:
In formula: Q-HRR, MW;
E
1the heat that-consumption unit volume oxygen discharges, 17.3MJ/m
3;
the environment mole percentage of-oxygen, %;
Φ-coefficient of oxygen consuming;
The oxygen consumption spreading coefficient of α-combustion reaction, α=1.105;
cO in-air
2concentration, %;
cO in-flue gas
2concentration, %;
X
cO-CO concentration in flue gas, %.
The above is only preferred implementation of the present utility model; it should be noted that; for those skilled in the art; under the prerequisite not departing from the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (8)
1. a multi-channel parallel heat release rate testing system, is characterized in that, comprises firing chamber, data acquisition unit, data processor and multiple test cell; Each described test cell comprises gas collection system, flue gas flow measuring system and flue gas sampling system, and described gas collection system comprises smoke discharging pipe, honeycomb screen, sampling section and smoke exhaust fan; Described flue gas flow measuring system comprises two-way pitot tube, differential pressure pick-up and thermopair; Described flue gas sampling system comprises flue gas sampling pipe, condenser, smoke filter, drying device, sampling pump, spinner-type flowmeter, lambda sensor, CO
2sensor, CO sensor; Described smoke discharging pipe is respectively by exhaust opening and described combustion chamber, and the described smoke discharging pipe in each described test cell is connected in parallel; Described sampling section is arranged at the described well-mixed position of smoke discharging pipe inside smoke, and it is inner that described honeycomb screen is installed on described smoke discharging pipe, and described smoke exhaust fan is installed on the endpiece of described smoke discharging pipe; Be provided with described two-way pitot tube, thermopair and flue gas sampling pipe in described sampling section, described two-way pitot tube is connected with described differential pressure pick-up; The flue gas output terminal of described flue gas sampling pipe successively with described condenser, smoke filter, drying device, sampling pump, spinner-type flowmeter, lambda sensor, CO
2sensor is connected with CO sensor, described thermopair, differential pressure pick-up, lambda sensor, CO
2sensor is connected with the signal input part of described data acquisition unit respectively with the signal output part of CO sensor, and the signal output part of described data acquisition unit is connected with the signal input part of described data processor.
2. multi-channel parallel heat release rate testing system according to claim 1, it is characterized in that, described exhaust opening is positioned at the sidewall of described firing chamber, and the smoke discharging pipe of each described test cell be arranged in parallel with described firing chamber respectively.
3. multi-channel parallel heat release rate testing system according to claim 2, it is characterized in that, described burner ends is separately installed with smoke-proof pendant wall.
4. multi-channel parallel heat release rate testing system according to claim 1, it is characterized in that, described exhaust opening is positioned at the top of described firing chamber, and the smoke discharging pipe of each described test cell is respectively by described exhaust opening and described combustion chamber.
5. multi-channel parallel heat release rate testing system according to claim 4, it is characterized in that, described burner ends is separately installed with smoke-proof pendant wall.
6. the multi-channel parallel heat release rate testing system according to any one of claim 1-5, is characterized in that, described two-way pitot tube is installed on the center line of described smoke discharging pipe.
7. multi-channel parallel heat release rate testing system according to claim 6, it is characterized in that, described lambda sensor adopts zirconia sensor, the probe segment of described zirconia sensor is installed in metallic test chamber, described zirconia sensor is with heating element, and described heating element is connected with direct supply.
8. multi-channel parallel heat release rate testing system according to claim 7, is characterized in that, be provided with three-way connection between described sampling pump and spinner-type flowmeter, the arm of described three-way connection is communicated with external environment condition; Described smoke exhaust fan is connected with frequency converter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520250732.6U CN204556552U (en) | 2015-04-23 | 2015-04-23 | A kind of multi-channel parallel heat release rate testing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520250732.6U CN204556552U (en) | 2015-04-23 | 2015-04-23 | A kind of multi-channel parallel heat release rate testing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204556552U true CN204556552U (en) | 2015-08-12 |
Family
ID=53831646
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520250732.6U Expired - Fee Related CN204556552U (en) | 2015-04-23 | 2015-04-23 | A kind of multi-channel parallel heat release rate testing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204556552U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104764769A (en) * | 2015-04-23 | 2015-07-08 | 天津商业大学 | Multichannel parallel heat release rate test system and test method |
| CN106198092A (en) * | 2016-09-12 | 2016-12-07 | 公安部四川消防研究所 | A kind of heat extraction performance test methods of fume control system |
| CN106323661A (en) * | 2016-09-12 | 2017-01-11 | 公安部四川消防研究所 | Testing method of tunnel smoke vent opening concentrated smoke evacuation performance testing device |
-
2015
- 2015-04-23 CN CN201520250732.6U patent/CN204556552U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104764769A (en) * | 2015-04-23 | 2015-07-08 | 天津商业大学 | Multichannel parallel heat release rate test system and test method |
| CN106198092A (en) * | 2016-09-12 | 2016-12-07 | 公安部四川消防研究所 | A kind of heat extraction performance test methods of fume control system |
| CN106323661A (en) * | 2016-09-12 | 2017-01-11 | 公安部四川消防研究所 | Testing method of tunnel smoke vent opening concentrated smoke evacuation performance testing device |
| CN106323661B (en) * | 2016-09-12 | 2018-08-31 | 公安部四川消防研究所 | A kind of test method of tunnel smoke outlet central exhaust performance testing device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104764769A (en) | Multichannel parallel heat release rate test system and test method | |
| CN203981700U (en) | Dust through-current capacity pick-up unit | |
| CN106971666A (en) | A kind of multi-functional underground railway tunnel fire ventilation smoke exhaust pattern simulation research platform | |
| CN201307109Y (en) | Multi-parameter coupling fire spread tester | |
| CN103323273B (en) | A kind of method detecting power station boiler air pre-heater performance | |
| CN204556552U (en) | A kind of multi-channel parallel heat release rate testing system | |
| CN109099001B (en) | Method for measuring efficiency of induced draft fan of power station boiler | |
| CN104807500B (en) | The warehouse separated type air preheater method for testing performance of large-sized station boiler three | |
| CN205941424U (en) | Heat of combustion rate of release test system under low pressure environment | |
| CN107917736A (en) | A kind of domestic stove flue gas pollutant discharges filed detection system | |
| CN106197517A (en) | A kind of Dual-Phrase Distribution of Gas olid simulating test device and relative concentration method of calibration | |
| CN104777189B (en) | A kind of oxygen-enriched combusting assesses experimental provision | |
| CN106442857A (en) | Detection method and detection device for carbon dioxide emission based on oxygen content determination | |
| CN202853655U (en) | Flue gas monitoring system | |
| CN104748995B (en) | The simulation testing device of system reliability control characteristic is utilized for smoke discharging residual heat | |
| CN109682714B (en) | Pile body resistance measuring device and resistance coefficient obtaining method | |
| CN205958413U (en) | Gas -solid two -phase flow simulating measurement setup | |
| CN206038383U (en) | A net multi -point sampling system for monitoring of multi -phase fluid medium composition | |
| CN209764640U (en) | Pile resistance measuring device | |
| Scholtens et al. | Improved passive flux samplers for measuring ammonia emissions from animal houses, part 1: basic principles | |
| CN208606585U (en) | For smoke exhaust fan high temperature resistant trial furnace | |
| Bryant | Uncertainty estimates of tracer gas dilution flow measurements in large-scale exhaust ducts | |
| CN201540239U (en) | Wind tunnel system for detecting dynamic aerosol | |
| CN208818670U (en) | A kind of portable dual oxide zirconium probe flue gas humidity monitoring device | |
| CN203658110U (en) | Gas-solid two-phase flow sampling device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150812 Termination date: 20160423 |