CN204789071U - Portable pollution sources dilute passageway aerosol sampling device and fluidization cabin - Google Patents
Portable pollution sources dilute passageway aerosol sampling device and fluidization cabin Download PDFInfo
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- CN204789071U CN204789071U CN201520195399.3U CN201520195399U CN204789071U CN 204789071 U CN204789071 U CN 204789071U CN 201520195399 U CN201520195399 U CN 201520195399U CN 204789071 U CN204789071 U CN 204789071U
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- 238000005070 sampling Methods 0.000 title claims abstract description 102
- 239000000443 aerosol Substances 0.000 title claims abstract description 38
- 238000005243 fluidization Methods 0.000 title abstract 5
- 230000000694 effects Effects 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 238000004891 communication Methods 0.000 claims abstract description 8
- 239000007789 gas Substances 0.000 claims description 95
- 239000002245 particle Substances 0.000 claims description 66
- 239000012159 carrier gas Substances 0.000 claims description 15
- 238000010790 dilution Methods 0.000 claims description 15
- 239000012895 dilution Substances 0.000 claims description 15
- 239000003085 diluting agent Substances 0.000 claims description 6
- 238000009833 condensation Methods 0.000 claims description 5
- 230000005494 condensation Effects 0.000 claims description 5
- 239000011521 glass Substances 0.000 claims description 3
- 238000005498 polishing Methods 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000000926 separation method Methods 0.000 abstract description 4
- 239000013618 particulate matter Substances 0.000 abstract 3
- 239000000523 sample Substances 0.000 description 76
- 230000003189 isokinetic effect Effects 0.000 description 25
- 238000005516 engineering process Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 3
- 239000012470 diluted sample Substances 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 230000003068 static effect Effects 0.000 description 3
- 239000003500 flue dust Substances 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Sampling And Sample Adjustment (AREA)
Abstract
The utility model provides a portable pollution sources dilute passageway aerosol sampling device and fluidization cabin, including the sampling mouth, the sampling pipe, the pitot tube, heating device, the diluter, the particulate matter cutterbar, the fluidization cabin, the desicator, a filte, the tee bend, the solenoid valve, the aspiration pump, the circulating air return circuit, a single -chip microcomputer, pipeline temperature sensor ts, pipeline pressure sensor ps, pitot tube differential pressure sensor triangle P1, temperature sensor tg, temperature sensor tc, pressure sensor pc, flow sensor qc, pressure sensor pr, flow sensor qr, the keyboard, the display, communication interface. The utility model discloses can dilute the sample gas of high temperature, high humility, high concentration in the pipeline, realize sampling of sample gas constant speed and particulate matter constant current separation, with the aerosol sample collection in the pipeline to the fluidization cabin in, at the fluidization under -deck, the particulate matter is overcome the gravitational settling effect and is in flow state in the aerosol.
Description
Technical field
The utility model relates to a kind of portable pollution source dilution tunnel aerosol sampling apparatus and fluidized cabin, belongs to environment monitoring instrument field.
Background technology
When gathering aerosol sample from discharge of pollutant sources pipeline (hereinafter referred to as pipeline), because the humidity of gas in pipelines, temperature are higher than ambient humidity, temperature, many dynamic physical chemical dynamics processes (nucleogenesis, coagulation, compression etc.) and chemical process can be there is in sampling system, affect sampled result.For avoiding change of size and the sample gas components change of particle in sample gas in sampling process, obtaining representational monitoring result, the temperature of high temperature, high humidity and high concentration sample gas in pipeline, humidity and concentration must be reduced post-sampling.
The aerosol sample gathering specified particle diameter from pipeline is delivered in the process of laboratory automatic analytical instrument analysis, and the technical measures of needs also comprise: implement isokinetic sampling's technology and gather ducted aerosol sample; The particle of specified particle diameter is separated by application cutter for particles from sample gas; Contained by the aerosol sample collected and take back laboratory analysis in a vessel, period, aerosol sample should be in suspended state in a reservoir.Prior art can not complete above-mentioned requirements simultaneously.
Existing technology is:
1. dilution after being taken out in pipeline by sample gas with fluidics, collected specimens after sample air humidity degree, temperature, concentration are reduced, shortcoming is when adopting fluidics, and sampling flow velocity can not follow the tracks of gas in pipelines change in flow.Therefore, isokinetic sampling cannot be realized.
2. existing smoke dust sampling instrument can utilize isokinetic sampling's technology to gather aerosol sample, but particle can not be pressed particle diameter separation, and can not solve high temperature, high humidity sample gas condensation trouble.Therefore, the aerosol sample of specified particle diameter can not be separated by prior art from sample gas, cannot gather the aerosol sample of specified particle diameter.
3. utilize the specific particle in cutter for particles separation sample gas, require that the sample gas velocity entering cutter for particles is constant, and during isokinetic sampling, from the change of motion tracking gas in pipelines flow velocity, isokinetic sampling must be implemented, namely when gas in pipelines change in flow, the sample gas velocity entering cutter for particles also changes, thus isolated particle size is uncertain, and changes with the change of sample gas velocity, can not obtain desirable sample.
4. utilize airbag to gather aerosol sample, because sampling location is distant to laboratory, sample being delivered to laboratory from scene generally needs 2 ~ 3 hours, and in transportation, the particle in sample gas is deposited in airbag because of gravity settling reason.Therefore, enough suspended sample cannot be provided for analytical instrument.
Utility model content
Technical problem to be solved in the utility model is for the deficiency existing for prior art, a kind of portable pollution source dilution tunnel aerosol sampling apparatus and fluidized cabin are provided, utilize pitot tube isokinetic sampling principle, utilize diluter, cutter for particles, circulating air loop and pressure, differential pressure, temperature, flow sensor and scm observe and control technology, the function that in pipeline, sample gas isokinetic sampling is separated with particle constant current can be realized, aerosol sample in pipeline is collected in fluidized cabin, in fluidized cabin, the molten middle glue aerosol sample of gas overcomes gravity settling effect, be suspended in fluidized cabin.
In order to solve the problems of the technologies described above, the technical solution of the utility model is: a kind of portable pollution source dilution tunnel aerosol sampling apparatus and fluidized cabin, comprising: sampling mouth, sampling pipe, pitot tube, heating arrangement, diluter, cutter for particles, fluidized cabin, exsiccator, filtrator, threeway, solenoid valve, aspiration pump, circulating air loop, single-chip microcomputer, Tube Temperature Sensor T
s, pipe pressure sensor P
s, pitot tube differential pressure pick-up △ P
1, temperature sensor T
g, temperature sensor T
c, pressure transducer P
c, flow sensor Q
c, pressure transducer P
r, flow sensor Q
r, keyboard, display, communication interface; Described sampling mouth, sampling pipe, diluter, cutter for particles, fluidized cabin, exsiccator, filtrator, flow sensor Q
c, threeway, flow sensor Q
r, solenoid valve, aspiration pump connect successively.
Further, described pitot tube and pipe pressure sensor P
s, pitot tube differential pressure pick-up △ P
1connect; Described Tube Temperature Sensor T
s, pipe pressure sensor P
s, pitot tube differential pressure pick-up △ P
1all electrically connect with single-chip microcomputer.
Further, described sampling pipe can be made up of interior polishing stainless steel pipe or glass, sampling pipe one termination sampling mouth, another termination diluter; Sampling pipe outer wall is installed heating arrangement and temperature sensor T
g; Described temperature sensor T
gelectrically connect with single-chip microcomputer; Described heating arrangement carries out heating and thermal insulation to sample gas in sampling pipe, prevents the sample gas of high temperature in pipeline, high humidity to lower the temperature on sampling pipe inwall condensation, the form of sample gas and composition are changed.
Further, described diluter is made up of sample gas air intake opening, carrier gas air intake opening, gas outlet and shell; Sample gas air intake opening stretches into diluter inside; Carrier gas air intake opening is arranged on shell, communicates with diluter inside; Gas outlet is arranged on end cap, communicates with diluter inside.
Further, the sample gas air intake opening of diluter connects with sampling pipe, and carrier gas air intake opening connects circulating air loop, and gas outlet connects cutter for particles.
Further, described cutter for particles porch is provided with temperature sensor T
c, pressure transducer P
c, described temperature sensor T
c, pressure transducer P
call electrically connect with single-chip microcomputer.
Further, described fluidized cabin is the closed container of a hollow, is provided with fan in fluidized cabin, and fluidized cabin draft tube is provided with gas admittance valve, and fluidized cabin escape pipe is provided with air outlet valve.
Further, be provided with ebullator in described circulating air loop, the gas outlet of ebullator is connected on the carrier gas air intake opening of diluter by pipeline, and the air intake opening of ebullator is parallel in threeway by pipeline; Under the effect at ebullator of the dry state diluents of exsiccator, filtrator dry filter, enter in diluter by circulating air loop, diluted by sample gas, the humidity of sample gas, temperature are reduced, when avoiding sample gas to enter cutter for particles, the form of sample gas components and particle changes.
Further, described pressure transducer P
rbe arranged on flow sensor Q
rbefore, before described motorized valve is arranged on aspiration pump; Described flow sensor Q
c, pressure transducer P
r, flow sensor Q
r, solenoid valve all electrically connects with single-chip microcomputer.
Further, described keyboard, display, communication interface, aspiration pump and ebullator all electrically connect with single-chip microcomputer.
Further, isokinetic sampling to be achieved in that the dynamic pressure in pipeline, static pressure by pitot tube through pipe pressure sensor P
s, pitot tube differential pressure pick-up △ P
1reach single-chip microcomputer, single-chip microcomputer is according to pitot tube differential pressure pick-up △ P
1measured value calculates the flow velocity in pipeline, and according to temperature sensor T in the sampling diameter of mouth and pipeline
sthe temperature value recorded calculates isokinetic sampling's flow value q
r', control the rotating speed of aspiration pump, make by flow sensor Q
rflow value Q
r' with isokinetic sampling's flow value q
r' equal, implement isokinetic sampling.
Further, particle constant current is separated and is achieved in that after selecting cutter for particles, working point flow value q
cjust fixedly determine, therefore, require that by the gas flow values of cutter for particles be constant, this value is realized by the rotating speed of Single-chip Controlling aspiration pump and ebullator.Cutter for particles working point flow q
cequal isokinetic sampling's flow value q
r' with circulating air loop stream value q
xsum, i.e. q
c=q
r'+q
x, wherein: q
r' value is isokinetic sampling's flow value, q
cvalue is according to flow sensor Q by single-chip microcomputer
cthe flow value recorded, temperature sensor T
cthe temperature value recorded and pressure transducer P
cthe force value recorded calculates.During sampling, under the effect of aspiration pump and ebullator, ducted sample gas enters in diluter through sampling mouth, sampling pipe, meanwhile, the diluents provided by closed circuit enters in diluter through carrier gas draft tube, diluted by sample gas, diluted sample gas enters cutter for particles through the escape pipe of diluter, and single-chip microcomputer is according to the cutter for particles working flow point q of setting
cwith isokinetic sampling's flow value q
r' difference q
x=q
c-q
r', the rotating speed of controlled circulation pump, makes by flow sensor Q
cflow value and the working point flow q of setting
cequal, realize particle constant current and be separated.
The beneficial effects of the utility model are: 1, utilize diluter by after the gas processing of high humidity, high temperature, high concentration, can collect aerosol sample; 2, utilize cutter for particles can remove the particle of Large stone, realize particle constant current and be separated, aerosol sample is collected in fluidized cabin; 3, fluidized cabin can make aerosol sample in the gasoloid collected overcome gravity settling effect and be in flow state, is suspended in fluidized cabin; 4, can isokinetic sampling be realized, the total release of pipeline pollutant can be calculated; 5, lightweight, be convenient for carrying, simple to operate, automation and intelligentification level is high.Device of the present utility model is also applicable to gather harmful gas, flue dust, SVOCs sample and the surrounding air in pipeline.
Accompanying drawing explanation
Fig. 1 is structural principle schematic diagram of the present utility model;
Fig. 2 is diluter structural representation of the present utility model.
1. sampling mouth; 2. sampling pipe; 3. pitot tube; 4. heating arrangement; 5. Tube Temperature Sensor T
s; 6. pipeline road pressure transducer P
s; 7. pitot tube differential pressure pick-up △ P
1; 8. temperature sensor T
g; 9. diluter; 10. temperature sensor T
c; 11. pressure transducer P
c; 12. cutter for particles; 13. gas admittance valves; 14. fluidized cabins; 15. fans; 16. air outlet valves; 17. exsiccators; 18. filtrators; 19. flow sensor Q
c; 20. threeways; 21. pressure transducer P
r; 22. flow sensor Q
r; 23. solenoid valves; 24. aspiration pumps; 25. circulating air loops; 26. ebullators; 27. single-chip microcomputers; 28. keyboards; 29. displays; 30. communication interfaces; 31. sample gas air intake openings; 32. carrier gas air intake openings; 33. shells; 34. gas outlets.
Embodiment
Below in conjunction with accompanying drawing 1, accompanying drawing 2 and embodiment, the utility model is further illustrated.
As shown in Figure 1 and Figure 2, a kind of portable pollution source dilution tunnel aerosol sampling apparatus and fluidized cabin, comprising: sampling mouth 1, sampling pipe 2, pitot tube 3, heating arrangement 4, diluter 9, cutter for particles 12, fluidized cabin 14, exsiccator 17, filtrator 18, threeway 20, solenoid valve 23, aspiration pump 24, circulating air loop 25, single-chip microcomputer 27, Tube Temperature Sensor T
s5, pipe pressure sensor P
s6, pitot tube differential pressure pick-up △ P
17, temperature sensor T
g8, temperature sensor T
c10, pressure transducer P
c11, flow sensor Q
c19, pressure transducer P
r21, flow sensor Q
r22, keyboard 28, display 29, communication interface 30; Described sampling mouth 1, sampling pipe 2, diluter 9, cutter for particles 12, fluidized cabin 14, exsiccator 17, filtrator 18, flow sensor Q
c19, threeway 20, flow sensor Q
r22, solenoid valve 23, aspiration pump 24 are connected successively.
Pitot tube 3 and pipe pressure sensor P
s6, pitot tube differential pressure pick-up △ P
17 connect; Tube Temperature Sensor T
s5, pipe pressure sensor P
s6, pitot tube differential pressure pick-up △ P
17 all electrically connect with single-chip microcomputer 27, for the parameter such as temperature, dynamic pressure, static pressure, flow velocity of measuring channel.
Sampling pipe 2 inner wall smooth, to reduce the wall loss of sample, available interior polishing stainless steel pipe or glass are made, sampling pipe 2 one termination sampling mouth 1, another termination diluter 9; Sampling pipe 2 outer wall is installed heating arrangement 4 and temperature sensor T
g8, temperature sensor T
g8 electrically connect with single-chip microcomputer 27.During work, under the effect of aspiration pump 24, sample gas enters in diluter 9 by sampling mouth 1, sampling pipe 2 from pipeline, to lower the temperature on sampling pipe 2 inwall condensation for preventing the sample gas of high temperature in pipeline, high humidity, the form of sample gas and composition are changed, and in heating arrangement 4 pairs of sampling pipes 2, sample gas carries out heating and thermal insulation.According to temperature sensor T
gsample temperature degree in 8 sampling pipes recorded 2, single-chip microcomputer 27 observing and controlling heating arrangement 4 heats or stops heating, makes temperature value and Tube Temperature Sensor T in sampling pipe 2
sthe 5 pipe temperature values recorded are equal, in order to avoid sample gas is because of cooling condensation.
Diluter 9 is made up of sample gas air intake opening 31, carrier gas air intake opening 32, gas outlet 34 and shell 33; It is inner that sample gas air intake opening 31 stretches into diluter 9; Carrier gas air intake opening 32 is arranged on shell 33, communicates with diluter 9 inside; Gas outlet 34 is arranged on end cap, communicates with diluter 9 inside.
The sample gas air intake opening 31 of diluter 9 connects with sampling pipe 2, and carrier gas air intake opening 32 connects circulating air loop 25, and gas outlet 34 connects cutter for particles 12.
Cutter for particles 12 porch is provided with temperature sensor T
c10, pressure transducer P
c11, described temperature sensor T
c10, pressure transducer P
c11 all electrically connect with single-chip microcomputer 27, measure temperature, the pressure of cutter for particles 12 porch, participate in the gas operating mode flow calculated by cutter for particles 12.
Fluidized cabin 14 is closed containers of a hollow, the draft tube of fluidized cabin 14 is provided with gas admittance valve 13, the escape pipe of fluidized cabin 14 is provided with air outlet valve 16, is provided with fan 15 in fluidized cabin 14.The effect of fan 15 ensures that the aerosol particle matter sample in fluidized cabin 14 can keep flow state, is suspended in air-flow, avoids because Action of Gravity Field produces sedimentation.
Exsiccator 17 is for the sample gas in dry gas circuit, and filtrator 18 is for filtering the sample gas in gas circuit.
Circulating air loop 25 is provided with ebullator 26, the gas outlet of ebullator 26 is connected on the carrier gas air intake opening 32 of diluter 9 by pipeline, and the air intake opening of ebullator 26 is parallel in threeway 20 by pipeline.Dry state diluents through exsiccator 17, filtrator 18 dry filter enters in diluter 9 by circulating air loop 25 under the effect of ebullator 26, sample gas is diluted, the humidity of sample gas, temperature are reduced, and when avoiding sample gas to enter cutter for particles 12, the form of sample gas components and particle changes.
Flow sensor Q
c19 electrically connect with single-chip microcomputer 27, and measured value participates in the operating mode flow calculated by the sample gas of cutter for particles 12.
Pressure transducer P
r21 are arranged on flow sensor Q
rbefore 22; Pressure transducer P
r21, flow sensor Q
r22 all electrically connect with single-chip microcomputer 27, measure by flow sensor Q
rmark condition flow, the pressure of the sample gas of 22, participate in and calculate by flow sensor Q
rthe operating mode flow of the sample gas of 22.
Before solenoid valve 23 is arranged on aspiration pump 24, during for checking the sealing of gas circuit, be in closure state; Unimpeded state is in during sampling.
Keyboard 28, display 29, communication interface 30, aspiration pump 24 and ebullator 26 all electrically connect with single-chip microcomputer 27.
Isokinetic sampling to be achieved in that the dynamic pressure in pipeline, static pressure by pitot tube 3 through pipe pressure sensor P
s6, pitot tube differential pressure pick-up △ P
17 reach single-chip microcomputer 27, and single-chip microcomputer 27 is according to pitot tube differential pressure pick-up △ P
17 measured values calculate the flow velocity in pipeline, and according to temperature sensor T in the sampling diameter of mouth 1 and pipeline
s5 temperature values recorded calculate isokinetic sampling's flow value q
r', control the rotating speed of aspiration pump 24, make by flow sensor Q
rthe flow value Q of 22
r' with isokinetic sampling's flow value q
r' equal, implement isokinetic sampling.
Particle constant current is separated and is achieved in that after selecting cutter for particles 12, working point flow value q
cjust fixedly determine, therefore, require that by the gas flow values of cutter for particles 12 be constant, the rotating speed that this value controls aspiration pump 24 and ebullator 26 by single-chip microcomputer 27 realizes.Cutter for particles working point flow q
cequal isokinetic sampling's flow value q
r' with circulating air loop stream value q
xsum, i.e. q
c=q
r'+q
x, wherein: q
r' value is isokinetic sampling's flow value, q
cvalue is according to flow sensor Q by single-chip microcomputer 27
c19 mark condition flow value, the temperature sensor T recorded
c10 temperature values recorded and pressure transducer P
c11 force value recorded calculate.During sampling, under the effect of aspiration pump 24 and ebullator 26, ducted sample gas enters in diluter 9 through sampling mouth 1, sampling pipe 2, meanwhile, the diluents provided by closed circuit 25 enters in diluter 9 through carrier gas draft tube 32, diluted by sample gas, diluted sample gas enters cutter for particles 12 through the escape pipe 34 of diluter 9, and single-chip microcomputer 27 is according to the cutter for particles working flow point q of setting
cwith isokinetic sampling's flow value q
r' difference q
x=q
c-q
r', the rotating speed of controlled circulation pump 26, makes by flow sensor Q
cthe flow value of 19 and the working point flow q of setting
cequal, realize particle constant current and be separated.
During sampling, open gas admittance valve 13, air outlet valve 16, under the effect of aspiration pump 24, sample gas is drawn out of from pipeline, by sampling mouth 1, sampling pipe 2 enters in diluter 9, meanwhile, through exsiccator 17, filtrator 18 is dry, the dry state diluents filtered enters in diluter 9 by circulating air loop 25 under the effect of ebullator 26, sample gas is diluted, the humidity of diluted sample gas, after temperature and concentration all decrease, enter cutter for particles 12, in cutter for particles 12, according to aerodynamic principle, utilize the inertia of particle by particulate separation, the inertia of the bulky grain thing in air-flow is large, flee from air-flow through air-flow and be removed, collected aerosol particle matter sample stays in the gas flow because inertia is little, and with air motion, enter in fluidized cabin 14.
When the flow velocity in pipeline increases, pitot tube 3 records signal and reaches single-chip microcomputer 27, and single-chip microcomputer 27 is according to the corresponding discharge calculated, and the rotating speed controlling aspiration pump 24 increases, and makes by flow sensor Q
rthe flow value of 22 is increased to isokinetic sampling's flow value q
r', realize isokinetic sampling; Meanwhile, reduced by the rotating speed of single-chip microcomputer 27 controlled circulation pump 26, make flow sensor Q
cthe working point flow value q of 19 flow values recorded and setting
cequal, achieve particle constant current and be separated; Otherwise, as the same.
After sampling terminates, close air outlet valve 16 and gas admittance valve 13, aerosol sample is collected to be kept in fluidized cabin 14, fluidized cabin 14 is taken off, after starting fan 15, the aerosol particle matter sample in fluidized cabin, under the effect of fan 15, keeps flow state in fluidized cabin 14, thus overcome gravity settling effect, be suspended in fluidized cabin 14.When being chemically examined by sample, opened by air outlet valve 16, draw samples in fluidized cabin 14, send analytical instrument analytical test.
Device of the present utility model is also applicable to gather harmful gas, flue dust, SVOCs sample and the surrounding air in pipeline.
In sum, the utility model utilizes air mix facilities can by after the gas processing of high humidity, high temperature, high concentration, utilize cutter for particles can remove the particle of Large stone, realize particle constant current to be separated, aerosol sample is collected in fluidized cabin, fluidized cabin can make aerosol sample in the gasoloid collected overcome gravity settling effect, is in flow state, is suspended in fluidized cabin; Can isokinetic sampling be realized, the total release of pipeline pollutant can be calculated; Lightweight, be convenient for carrying; Simple to operate, automation and intelligentification level is high.
Be illustrated the utility model by way of example above, but the utility model is not limited to above-mentioned specific embodiment, all any changes of doing based on the utility model or modification all belong to the claimed scope of the utility model.
Claims (9)
1. a portable pollution source dilution tunnel aerosol sampling apparatus and fluidized cabin, it is characterized in that: comprising: sampling mouth, sampling pipe, pitot tube, heating arrangement, diluter, cutter for particles, fluidized cabin, exsiccator, filtrator, threeway, solenoid valve, aspiration pump, circulating air loop, single-chip microcomputer, Tube Temperature Sensor Ts, pipe pressure sensor Ps, pitot tube differential pressure pick-up △ P1, temperature sensor Tg, temperature sensor Tc, pressure transducer Pc, flow sensor Qc, pressure transducer Pr, flow sensor Qr, keyboard, display, communication interface, described sampling mouth, sampling pipe, diluter, cutter for particles, fluidized cabin, exsiccator, filtrator, flow sensor Qc, threeway, flow sensor Qr, solenoid valve, aspiration pump are connected successively.
2. portable pollution source dilution tunnel aerosol sampling apparatus according to claim 1 and fluidized cabin, is characterized in that: sampling pipe inner wall smooth, can be made up of interior polishing stainless steel pipe or glass, sampling pipe one termination sampling mouth, another termination diluter; Sampling pipe outer wall is installed heating arrangement and temperature sensor Tg; Described temperature sensor Tg and single-chip microcomputer electrically connect; Described heating arrangement is incubated sample gas in sampling pipe, and before preventing the sample gas of high temperature in pipeline, high humidity from entering diluter, condensation that sampling pipe inwall is lowered the temperature, makes sample gas change.
3. portable pollution source dilution tunnel aerosol sampling apparatus according to claim 1 and fluidized cabin, is characterized in that: described diluter is made up of sample gas air intake opening, carrier gas air intake opening, gas outlet and shell; Sample gas air intake opening stretches into diluter inside; Carrier gas air intake opening is arranged on shell, communicates with diluter inside; Gas outlet is arranged on end cap, communicates with diluter inside.
4. portable pollution source dilution tunnel aerosol sampling apparatus according to claim 3 and fluidized cabin, is characterized in that: the sample gas air intake opening of diluter connects with sampling pipe, and carrier gas air intake opening connects circulating air loop, and gas outlet connects cutter for particles.
5. portable pollution source dilution tunnel aerosol sampling apparatus according to claim 1 and fluidized cabin, it is characterized in that: described cutter for particles porch is provided with temperature sensor Tc, pressure transducer Pc, described temperature sensor Tc, pressure transducer Pc all electrically connect with single-chip microcomputer.
6. portable pollution source dilution tunnel aerosol sampling apparatus according to claim 1 and fluidized cabin, it is characterized in that: described fluidized cabin is the closed container of a hollow, in fluidized cabin, fan is installed, fluidized cabin draft tube is provided with gas admittance valve, fluidized cabin escape pipe is provided with air outlet valve.
7. portable pollution source dilution tunnel aerosol sampling apparatus according to claim 1 and fluidized cabin, it is characterized in that: in described circulating air loop, ebullator is installed, the gas outlet of ebullator is connected on the carrier gas air intake opening of diluter by pipeline, and the air intake opening of ebullator is parallel in threeway by pipeline; Enter in diluter by circulating air loop under the effect at ebullator of the dry state diluents of exsiccator, filtrator dry filter, sample gas is diluted, the humidity of sample gas, temperature are reduced, and when avoiding sample gas to enter cutter for particles, the form of sample gas components and particle changes.
8. portable pollution source dilution tunnel aerosol sampling apparatus according to claim 1 and fluidized cabin, is characterized in that: before described pressure transducer Pr is arranged on flow sensor Qr, before described solenoid valve is arranged on aspiration pump; Described flow sensor Qc, pressure transducer Pr, flow sensor Qr, solenoid valve all electrically connect with single-chip microcomputer.
9. portable pollution source dilution tunnel aerosol sampling apparatus according to claim 1 and fluidized cabin, is characterized in that: described keyboard, display, communication interface, aspiration pump and ebullator all electrically connect with single-chip microcomputer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520195399.3U CN204789071U (en) | 2015-04-02 | 2015-04-02 | Portable pollution sources dilute passageway aerosol sampling device and fluidization cabin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520195399.3U CN204789071U (en) | 2015-04-02 | 2015-04-02 | Portable pollution sources dilute passageway aerosol sampling device and fluidization cabin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204789071U true CN204789071U (en) | 2015-11-18 |
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ID=54529090
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520195399.3U Expired - Fee Related CN204789071U (en) | 2015-04-02 | 2015-04-02 | Portable pollution sources dilute passageway aerosol sampling device and fluidization cabin |
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|---|---|
| CN (1) | CN204789071U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104764631A (en) * | 2015-04-02 | 2015-07-08 | 青岛高远光电测控技术有限公司 | Portable aerosol sampling device for pollution source dilution channel and fluidization cabin |
| CN108872033A (en) * | 2018-05-24 | 2018-11-23 | 香港理工大学深圳研究院 | The heterogeneous reaction activity measurement device and method of gaseous pollutant in atmospheric environment |
-
2015
- 2015-04-02 CN CN201520195399.3U patent/CN204789071U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104764631A (en) * | 2015-04-02 | 2015-07-08 | 青岛高远光电测控技术有限公司 | Portable aerosol sampling device for pollution source dilution channel and fluidization cabin |
| CN108872033A (en) * | 2018-05-24 | 2018-11-23 | 香港理工大学深圳研究院 | The heterogeneous reaction activity measurement device and method of gaseous pollutant in atmospheric environment |
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