CN201096663Y - High-pressure dust-containing gas sampling pressure-reducing device - Google Patents
High-pressure dust-containing gas sampling pressure-reducing device Download PDFInfo
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- CN201096663Y CN201096663Y CNU2007201694424U CN200720169442U CN201096663Y CN 201096663 Y CN201096663 Y CN 201096663Y CN U2007201694424 U CNU2007201694424 U CN U2007201694424U CN 200720169442 U CN200720169442 U CN 200720169442U CN 201096663 Y CN201096663 Y CN 201096663Y
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- 238000005070 sampling Methods 0.000 title claims abstract description 84
- 239000000428 dust Substances 0.000 title claims description 42
- 239000007789 gas Substances 0.000 claims abstract description 124
- 230000006837 decompression Effects 0.000 claims abstract description 40
- 208000028659 discharge Diseases 0.000 claims abstract description 21
- 239000002912 waste gas Substances 0.000 claims abstract description 11
- 150000001875 compounds Chemical class 0.000 claims description 35
- 239000003638 chemical reducing agent Substances 0.000 claims description 10
- 230000008602 contraction Effects 0.000 claims description 9
- 239000002245 particle Substances 0.000 abstract description 36
- 238000000034 method Methods 0.000 abstract description 10
- 230000001105 regulatory effect Effects 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 10
- 238000001514 detection method Methods 0.000 description 5
- 239000003345 natural gas Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- 238000003780 insertion Methods 0.000 description 3
- 230000037431 insertion Effects 0.000 description 3
- 230000003189 isokinetic effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005315 distribution function Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 206010013496 Disturbance in attention Diseases 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- XTKDAFGWCDAMPY-UHFFFAOYSA-N azaperone Chemical compound C1=CC(F)=CC=C1C(=O)CCCN1CCN(C=2N=CC=CC=2)CC1 XTKDAFGWCDAMPY-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
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Abstract
The utility model discloses a high pressure dirty gas sampling pressure relief device. The device is characterized in that the rear ends of a primary expansion chamber [3] and a secondary expansion chamber [7] are respectively provided with a surplus gas outlet connected with a primary discharge pipe [4] and a secondary discharge pipe [8], the discharge pipe [4] and the discharge pipe [8] are respectively connected with a pressure regulating valve [5] and a pressure regulating valve [9], the gas flows through a primary discharge gas pressure reducing valve [15] and a secondary discharge gas pressure reducing valve [16] after being displayed by a primary pressure regulating pressure gauge [13] and a secondary pressure regulating pressure gauge [14], and the decompressed gas is discharged into a waste gas conveying pipeline [17 ]; the sampled and analyzed gas in the discharge pipe (12) is displayed by a secondary sampled gas pressure gauge (20) and a flowmeter (21) and then is discharged by a secondary sampled gas discharge pressure reducing valve (22) for pressure reduction, so that the pressure of the sampled and analyzed gas is reduced to the pressure in the waste gas conveying pipeline (17). The pressure reducing device has little influence on the concentration and the particle size distribution of particles; the high-pressure gas with the pressure of 20MPa can be decompressed to normal pressure or below; can ensure that no liquid drop (water) is separated out in the decompression process.
Description
Technical field
The utility model is the particularly high pressure dust gas sampling and decompression device of the interior dust detection of high-pressure natural gas conveyance conduit of high pressure dust gas.Relate to measurement not to be covered of other class and piping system technical field.
Background technology
Because most of particle analyzers (aerosol spectrometer) are all operated under the situation of normal pressure or pressure not too high (less than 1MPa), and some high pressure dust gas, its pressure is generally all higher, as high-pressure natural gas conveyance conduit internal pressure, and can be up to 10MPa.Obviously, can't directly adopt particle analyzer to carry out check and analysis.So, in the online detection of high pressure dust gas, realize the online detection of high pressure dust gas, just must reduce pressure, to satisfy the requirement of particle analyzer to pressure to high-pressure natural gas.
Rule of thumb as can be known, general reduction valve, needle valve and flow regulating equipment bring very big error because of it produces serious particle loss in decompression process to check and analysis, thereby can't be applied to the sampling and decompression of high pressure dust gas.Kasper is low by (10 to dust content
-5P/cm
3), dust size is less than the high pressure nitrogen of 1 μ m, adopts the orifice plate pressure reduction structure to detect.But when dust size during greater than 1 μ m, particle loses quite serious near aperture, thereby influences the accuracy and the authenticity of detection architecture.Moreover the dust content in the real mesohigh dusty gas is generally all than height, and the dust size major part is also all greater than 1 μ m, so must design the new sampling and decompression device of a cover to satisfy the needs of high pressure dust-laden detection.
The utility model content
The purpose of this utility model when to be that design is a kind of be used for high pressure dust gas particularly dust detect in the high-pressure natural gas conveyance conduit with high pressure air reducing to normal pressure or below the 1MPa, particle loss is little, degree of accuracy is high high pressure dust gas sampling and decompression device.
Difficult point in view of above-mentioned high pressure dust gas decompression sampling, the technical scheme that the utility model proposes as shown in Figure 1, adopt one-level expanding chamber 3 to connect the method for compound expansion chamber 7 double expansions exactly, and compound expansion chamber 7 is from one-level expanding chamber 3 isokinetic samplings, then by secondary sampling pipe 10 from the compound expansion chamber moving taking-up portion gas such as 7 grades to particle analyzer 11 analyze.
Sampling and decompression device of the present utility model constitutes as shown in Figure 1, and it is made up of one-level sampling pipe 1, deceleration sampling pipe 2, one-level expanding chamber 3, one-level vent pipe 4, one-level sample guide pipe 6, compound expansion chamber 7, secondary vent pipe 8 and secondary sampling pipe 10.The front end of one-level expanding chamber 3 (is preceding with deceleration sampling pipe 2) is connected with deceleration sampling pipe 2, and the escape hole that its rear portion has certain diameter is connected with one-level vent pipe 4, is used to discharge unnecessary gas.The rear end of one-level expanding chamber 3 is connected with one-level sample guide pipe 6, and one-level sample guide pipe 6 inserts certain degree of depth in the one-level expanding chamber 3.Compound expansion chamber 7 its front ends are connected with one-level sample guide pipe 6, the rear end is connected with secondary sampling pipe 10, and secondary sampling pipe 10 inserts certain degree of depth in the compound expansion chamber 7, and 7 rear portions, compound expansion chamber have the escape hole and the secondary vent pipe 8 of certain diameter equally, are used to discharge unnecessary gas.
The rear end that is characterized in one-level expanding chamber [3] and compound expansion chamber [7] respectively has unnecessary gas discharge outlet and links to each other with secondary vent pipe [8] with one-level vent pipe [4], vent pipe [4] and vent pipe [8] connect pressure-regulating valve [5], pressure-regulating valve [9] respectively, and gas stream is discharged gas pressure reducer [15] and secondary discharge gas pressure reducer [16] through one-level after being shown by one-level pressure regulation tensimeter [13], secondary pressure regulation tensimeter [14], and post-decompression gas drains in the waste gas pipeline road [17]; After secondary sample gas tensimeter [20], flowmeter [21] show, discharge reduction valve [22] by the sampling analysis gas of vent pipe [12] and reduce pressure, make its pressure reduce to the interior pressure in waste gas pipeline road [17] by the secondary sample gas.
Wherein slow down sampling pipe 2 (seeing Fig. 3-1 and Fig. 3-2) gauge structure such as front portion employing or adopt the flaring structure, expansion half-angle β is 5 °-90 ° during flaring, numerical simulation structure and experiment show that airflow reflux is little, particle loss is few; It is the contraction section of a that there is one section contraction half-angle at the rear portion of deceleration sampling pipe 2, becomes taper, and the value of a is between 10 °-90 °, and the awl point communicates with the uniform internal diameter aperture, and the aperture of aperture is between 0.3-5mm.
One-level sample guide pipe 6 rear structures are similar to deceleration sampling pipe 2, and it is the contraction section of a that also there is one section contraction half-angle at its rear portion, becomes taper, and the value of a is between 10 °-90 °, and the awl point communicates with the uniform internal diameter aperture, and the aperture of aperture is between 0.3-5mm.
For ease of installing, deceleration sampling pipe 2 and one-level sample guide pipe 6 are processed as two parts, a part is a slowing-down structure 23, another part is an AND DEWATERING FOR ORIFICE STRUCTURE 24, and orifice plate is movable structure (as Fig. 6), when the operation operating mode changes, be convenient for changing the diameter of aperture, to be equipped with the AND DEWATERING FOR ORIFICE STRUCTURE 24 in various apertures certainly.Specifically be to adopt two flanges 25, flange 26 that slowing-down structure 23, AND DEWATERING FOR ORIFICE STRUCTURE 24 are linked together with one-level expanding chamber 3.The connected mode of one-level sample guide pipe 6 and compound expansion chamber 7 is with the connected mode of deceleration sampling pipe 2 with one-level expanding chamber 3.
Wherein the degree of depth in the one-level sample guide pipe 6 insertion one-level expanding chambers 3 and the degree of depth in the secondary sampling pipe insertion compound expansion chambers 7 10 are pressed preceding method and are calculated definite; The length of one-level expanding chamber 3 and compound expansion chamber 7 and internal diameter are also pressed preceding method and are calculated definite.
The contraction section at deceleration sampling pipe 2 and one-level sample guide pipe 6 rear portions, its advantage are to reduce the inertia impact loss of particle in the aperture vicinity.Simultaneously, with the collision of expanding chamber Gu Bi, flaring structure (as Fig. 7) is all adopted in one-level expanding chamber 3 and compound expansion chamber 7 when entering in the expanding chamber for reducing particle after aperture expands, and expanding half-angle γ during flaring is 9.5 °-90 °.
Caused in the deceleration sampling pipe 2 by one-level sampling pipe 1 through the dried high pressure dust gas of condensation, the adiabatic expansion during aperture of high pressure dust gas by deceleration sampling pipe 2 rear ends increases gas volume, and pressure reduces, and temperature is also reduced to minimum in moment; Post-decompression gases at high pressure continue to expand in one-level expanding chamber 3, decompression; The back is caused in the compound expansion chamber 7 by the one-level sample guide pipe 6 that sample rate equals gas stabilized speed in the one-level expanding chamber 3, and gas unnecessary in the one-level expanding chamber 3 is discharged; After one-level sample guide pipe 6 grades were moved and take out required sample gas from one-level expanding chamber 3, through its terminal aperture (similar deceleration sampling pipe 2), in the compound expansion chamber 7 of flowing through, decompression reexpanded; Carry out check and analysis by moving taking-up portion gas such as secondary sampling pipe 10 grades to particle analyzer 11 then, unnecessary gas is discharged by secondary vent pipe 8 and pressure-regulating valve 9; Gas is after testing discharged through vent pipe 12.
The rear end of one-level expanding chamber 3 and compound expansion chamber 7 respectively has unnecessary gas discharge outlet and links to each other with secondary vent pipe 8 with one-level vent pipe 4, from vent pipe 4 and 8 two strands of gases of discharging, respectively through pressure-regulating valve 5,9 pressure regulation (as Fig. 2), and by gas stream is through one-level discharge gas pressure reducer 15 and secondary discharge gas pressure reducer 16 after one-level pressure regulation tensimeter 13,14 demonstrations of secondary pressure regulation tensimeter, post-decompression gas drains in the waste gas pipeline road 17.
Discharging reduction valve 22 by the secondary sample gas by the sampling analysis gas of vent pipe 12 after secondary sample gas tensimeter 20, flowmeter 21 show reduces pressure, make its pressure reduce to pressure (generally being higher than environmental pressure) in the waste gas pipeline road 17 to produce gas delivery power.
In order to guarantee that the gas flow that one-level sample guide pipe 6 is gathered has reached steady state (SS), what be that one-level sample guide pipe 6 gathered is the gas during velocity-stabilization in the one-level expanding chamber 3, then requires reduce pressure distance between the aperture of the one-level at one-level sample guide pipe 6 front ends (is preceding with one-level sampling pipe 1 direction) and constant speed collapsible tube 2 rear portions
θ is the expansion half-angle (or claim jet half-angle) of gas through small holes, D
T1Diameter for one-level expanding chamber 3; It inserts the degree of depth L in the one-level expanding chamber 3
1〉=5D
T1In like manner the degree of depth L in its insertion compound expansion chamber 7 also should be satisfied in the position of secondary sampling pipe 10 in compound expansion chamber 7
2〉=5D
T2, the distance between the second depressurized aperture at its front end (is preceding with one-level sampling pipe 1 direction) and one-level sample guide pipe 6 rear portions
θ is the expansion half-angle (or claim jet half-angle) of gas through small holes.
Wherein slow down sampling pipe 2 and one-level sample guide pipe 6 is pipes of being reduced gradually by uniform cross section of flow area from front to back, and the aperture of its rear end makes the air-flow decompression; The length of one-level expanding chamber 3 and compound expansion chamber 7 is respectively more than or equal to deceleration sampling pipe 2 and one-level sample guide pipe 6 rear portion hole diameters 40 times, and the internal diameter of one-level expanding chamber 3 and compound expansion chamber 7 is then respectively more than or equal to 5 times of hole diameter.
Separate out the temperature when every grade of decompression all should make the temperature of decompression back gas be unlikely to drop to the formation drop for guaranteeing dripless in decompression process (water).Can adopt the insulation measure at every grade of level decompression aperture place.In fact, as seen from Figure 4, most possibly produce drop at low-temperature space, but this low-temperature space only is (6-8) times hole diameter apart from weak point, and this moment, gas velocity herein can be up to velocity of sound even supersonic speed, gas is quite short in the residence time of this section low-temperature space, is no more than 10
-4S.Therefore, the possibility that gas produces drop herein also is quite little, and is impossible substantially.
Cause in the deceleration sampling pipe 2 by one-level sampling pipe 1 through the dried high pressure dust gas of condensation, the end of deceleration sampling pipe 2 has the very little aperture of a diameter (as Fig. 3), gas adiabatic expansion when high pressure dust gas passes through this hole, thereby gas volume is increased, pressure reduces, and temperature is also reduced to minimum in moment; Simultaneously, post-decompression gases at high pressure continue to expand in one-level expanding chamber 3, decompression.And in the distance of leaving aperture (6-8) times hole diameter, there is a low-temperature space in gas temperature, but very fast gas temperature can recover gradually, and in the distance of 40 times of hole diameters, gas temperature returns to the temperature (see figure 4) before expanding.Post-decompression gas part is caused in the compound expansion chamber 7 by one-level sample guide pipe 6.For guaranteeing that gas that one-level sample guide pipe 6 is gathered can represent the gas in the one-level expanding chamber 3, then require the isokinetic sampling, promptly sample rates equal the stabilized speed (see figure 5) of gases in the one-level expanding chamber 3 in the one-level sample guide pipe 6; Gas unnecessary in the one-level expanding chamber 3 is discharged through one-level vent pipe 4 and pressure-regulating valve 5.After one-level sample guide pipe 6 grades were moved and take out required sample gas from one-level expanding chamber 3, through its terminal aperture (similar deceleration sampling pipe 2), in the compound expansion chamber 7 of flowing through, decompression reexpanded.Thereby make through pressure after the two-stage decompression at the high pressure air reducing of 1MPa to 20MPa to normal pressure or below the 1MPa.Carry out check and analysis by moving taking-up portion gas such as secondary sampling pipe 10 grades to particle analyzer 11 then, unnecessary gas is discharged by secondary vent pipe 8 and pressure-regulating valve 9.Simultaneously, in order to reach the isokinetic sampling, must make secondary sampling pipe 10 interior sample rates equal the speed of gases in the compound expansion chamber 7.Gas is after testing discharged through vent pipe 12.
The utility model high pressure dust gas sampling and decompression device is little to the loss of particle, when particle diameter is 5 μ m, is lost in below 1%; When particle diameter was 10 μ m, loss was lower than 5%, and when particle diameter was 15 μ m, loss was lower than 10%.Particle diameter is 3.2 μ m in dust in addition, and dust distributes when obeying the Rosin-Rammler distribution function, and dust size is distributed almost not to be influenced.
In addition, separate out the temperature when every grade of decompression all should make the temperature of decompression back gas be unlikely to drop to the formation drop for guaranteeing dripless in decompression process (water).Can adopt the insulation measure at every grade of decompression aperture place.In fact, as seen from Figure 4, most possibly produce drop at low-temperature space, but this low-temperature space only is (6-8) times hole diameter apart from weak point, and this moment, gas velocity herein can be up to velocity of sound even supersonic speed, gas is quite short in the residence time of this section low-temperature space, is no more than 10
-4S.Therefore, the possibility that gas produces drop herein also is quite little, and is impossible substantially.
Be to analyze of the influence of the utility model high pressure dust gas sampling and decompression device, utilize the degree of dust relative concentration C (ratio of the concentration of dust when not losing of the concentration behind the dust loss) expression dust concentration loss dust concentration.The relative concentration of this device reaches as high as 98.74%, with actual error only be 1.26%.Minimum reaching is 97.11%, is no more than 3% with actual error.
Therefore characteristics of the present utility model are:
(1) this reliever is very little, promptly very little to the loss of particle to the concentration and the size distribution influence of particle, detects the degree of accuracy height;
(2) can be with pressure at the high pressure air reducing of 1MPa to 20MPa to normal pressure or below the 1MPa, be convenient to particle analyzer and under the situation of normal pressure or pressure not too high (less than 1MPa), operate;
(3) this reliever can guarantee that dripless in decompression process (water) separates out, in order to avoid reunite because of separating out of the globule with particle, and absorption, thus influence the concentration and the size distribution of particle.
Description of drawings
Fig. 1 high-pressure natural gas sampling and decompression schematic diagram of device
Fig. 2 reliever control flow chart
Fig. 3-1 deceleration sampling pipe 2 detail of construction
Fig. 3-2 front end has the deceleration sampling pipe figure of divergent segment
The temperature profile of Fig. 4 one-level decompression aperture vicinity
Velocity profile in Fig. 5 one-level expanding chamber
Fig. 6 sampling pipe 2 installations diagram that slow down
Fig. 7 I and II expanding chamber shape figure
Wherein:
1-one-level sampling pipe 2-deceleration sampling pipe
3-one-level expanding chamber 4 one-level vent pipes
5-pressure-regulating valve 6-one-level sample guide pipe
7-compound expansion chamber 8-secondary vent pipe
9-pressure-regulating valve 10-secondary sampling pipe
11-particle analyzer 12-vent pipe
13-one-level pressure regulation tensimeter 14-secondary pressure regulation tensimeter
The unnecessary discharge gas pressure reducer of the unnecessary discharge gas pressure reducer of 15-one-level 16-secondary
17-waste gas pipeline road 18-one-level is discharged gas and is taken over
The 19-secondary is discharged gas and is taken over 20-secondary sample gas tensimeter
21-flowmeter 22-secondary sample gas is discharged reduction valve
23-slowing-down structure 24-AND DEWATERING FOR ORIFICE STRUCTURE
25-flange 26-flange
Embodiment
Embodiment. embodiment of the present utility model is described and the utility model is further described with this example.It constitutes as shown in Figure 1-Figure 3.It is made up of one-level sampling pipe 1, deceleration sampling pipe 2, one-level expanding chamber 3, one-level vent pipe 4, one-level sample guide pipe 6, compound expansion chamber 7, secondary vent pipe 8 and secondary sampling pipe 10.The front end of one-level expanding chamber 3 (is preceding with deceleration sampling pipe 2) is connected with deceleration sampling pipe 2, and the escape hole that its rear portion has certain diameter is connected with one-level vent pipe 4, is used to discharge unnecessary gas.The rear end of one-level expanding chamber 3 is connected with one-level sample guide pipe 6, and one-level sample guide pipe 6 inserts certain degree of depth in the one-level expanding chamber 3.Compound expansion chamber 7 its front ends are connected with one-level sample guide pipe 6, the rear end is connected with secondary sampling pipe 10, and secondary sampling pipe 10 inserts certain degree of depth in the compound expansion chamber 7, and 7 rear portions, compound expansion chamber have the escape hole and the secondary vent pipe 8 of certain diameter equally, are used to discharge unnecessary gas.
Present embodiment is with the high pressure N of 10MPa (flow 50.871/min)
2Be decompressed to 0.4MPa, and this reliever is little to particle loss, the decompression process dripless produces.
Specifically being high pressure dust gas is caused in the deceleration sampling pipe 2 of φ 20mm by the one-level sampling pipe 1 of φ 6mm, the deceleration sampling pipe 2 anterior flaring structures that adopt, expansion half-angle β is 11 °, it is 22.5 ° that half-angle a is shunk at deceleration sampling pipe 2 rear portions, the end of deceleration sampling pipe 2 has the aperture of φ 2.4mm, and it is φ 45mm that high pressure dust gas enters internal diameter by this hole adiabatic expansion decompression, and the expansion half-angle is 9.5 °, length is that one-level expanding chamber 3 interior continuation of 500mm are expanded decompression.It is φ 42mm that post-decompression gas part causes internal diameter by the one-level sample guide pipe 6 (it is 22.5 ° that half-angle a is shunk at the rear portion) of φ 20mm, the expansion half-angle is that unnecessary gas is discharged through the one-level vent pipe 4 of φ 32mm and the pressure-regulating valve 5 of DN32 in 10 ° of length compound expansion chamber 7 that is 500mm.The gas of being introduced in the compound expansion chamber 7 by one-level sample guide pipe 6 (its terminal decompression hole diameter is φ 2.4mm) continues the decompression of expanding.Pressure is the high pressure N of 10MPa after two-stage decompression thereby make
20.4MPa reduces pressure.Moving taking-up portion gas such as secondary sampling pipe 10 grades by φ 6mm carries out check and analysis to particle analyzer 11 then, and unnecessary gas is discharged by secondary vent pipe 8 and the DN25 pressure-regulating valve 9 of φ 25mm.Gas is after testing discharged through the vent pipe 12 of φ 6mm.
Two strands of gases from one-level vent pipe 4 and 8 discharges of secondary vent pipe, respectively through pressure-regulating valve 5,9 pressure regulation (as Fig. 2), and by gas stream is through one-level discharge gas pressure reducer 15 and secondary discharge gas pressure reducer 16 after one-level pressure regulation tensimeter 13,14 demonstrations of secondary pressure regulation tensimeter, post-decompression gas drains in the waste gas pipeline road 17.
This example is through test of many times, prove can be with pressure at the high pressure air reducing of 1MPa to 20MPa to normal pressure or below the 1MPa, be convenient to particle analyzer and under the situation of normal pressure or pressure not too high (less than 1MPa), operate; Can guarantee that dripless in decompression process (water) separates out, in order to avoid reunite because of separating out of the globule with particle, absorption, thus influence the concentration and the size distribution of particle; Loss to particle is little, when particle diameter is 5 μ m, is lost in below 1%; When particle diameter was 10 μ m, loss was lower than 5%, and when particle diameter was 15 μ m, loss was lower than 10%.Particle diameter is 3.2 μ m in dust in addition, and dust distributes when obeying the Rosin-Rammler distribution function, and dust size is distributed almost not to be influenced; So concentration and size distribution influence to particle are very little, detect the degree of accuracy height.
Claims (5)
1. high pressure dust gas sampling and decompression device, it is made up of one-level sampling pipe [1], deceleration sampling pipe [2], one-level expanding chamber [3], one-level vent pipe [4], one-level sample guide pipe [6], compound expansion chamber [7], secondary vent pipe [8] and secondary sampling pipe [10], before with deceleration sampling pipe [2] being, the front end of one-level expanding chamber [3] is connected with deceleration sampling pipe [2], and the escape hole that its rear portion has certain diameter is connected with one-level vent pipe [4]; The rear end of one-level expanding chamber [3] is connected with one-level sample guide pipe [6], and one-level sample guide pipe [6] inserts certain degree of depth in the one-level expanding chamber [3]; Its front end of compound expansion chamber [7] is connected with one-level sample guide pipe [6], the rear end is connected with secondary sampling pipe [10], and secondary sampling pipe [10] inserts certain degree of depth in the compound expansion chamber [7], rear portion, compound expansion chamber [7] has the escape hole and the secondary vent pipe [8] of certain diameter equally, is used to discharge unnecessary gas; The rear end that it is characterized in that one-level expanding chamber [3] and compound expansion chamber [7] respectively has unnecessary gas discharge outlet and links to each other with secondary vent pipe [8] with one-level vent pipe [4], vent pipe [4] and vent pipe [8] connect pressure-regulating valve [5], pressure-regulating valve [9] respectively, and gas stream is discharged gas pressure reducer [15] and secondary discharge gas pressure reducer [16] through one-level after being shown by one-level pressure regulation tensimeter [13], secondary pressure regulation tensimeter [14], and post-decompression gas drains in the waste gas pipeline road [17]; After secondary sample gas tensimeter [20], flowmeter [21] show, discharge reduction valve [22] by the sampling analysis gas of vent pipe [12] and reduce pressure, make its pressure reduce to the interior pressure in waste gas pipeline road [17] by the secondary sample gas.
2. high pressure dust gas sampling and decompression device according to claim 1 is characterized in that the gauge structure or the flaring structures such as front portion employing of described deceleration sampling pipe [2], and expansion half-angle β is 5 °-90 ° during flaring; It is the contraction section of a that there is one section contraction half-angle at the rear portion of deceleration sampling pipe [2], becomes taper, and the value of a is between 10 °-90 °, and the awl point communicates with the uniform internal diameter aperture, and the aperture of aperture is between 0.3-5mm.
3. high pressure dust gas sampling and decompression device according to claim 1, it is characterized in that it is the contraction section of a that there is one section contraction half-angle at described one-level sample guide pipe [6] rear portion, become taper, the value of a is between 10 °-90 °, the awl point communicates with the uniform internal diameter aperture, and the aperture of aperture is between 0.3-5mm.
4. high pressure dust gas sampling and decompression device according to claim 1 is characterized in that described one-level expanding chamber [3] and compound expansion chamber [7] all adopt the flaring structure, and expansion half-angle γ is 9.5 °-90 ° during flaring.
5. high pressure dust gas sampling and decompression device according to claim 1, it is characterized in that slowing down sampling pipe [2] and one-level sample guide pipe [6] is made up of slowing-down structure [23] and AND DEWATERING FOR ORIFICE STRUCTURE [24] two parts, adopts two flanges [25], flange [26] that the AND DEWATERING FOR ORIFICE STRUCTURE [24] of slowing-down structure [23], bascule is linked together with one-level expanding chamber [3] or compound expansion chamber [7].
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201694424U CN201096663Y (en) | 2007-06-27 | 2007-06-27 | High-pressure dust-containing gas sampling pressure-reducing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201694424U CN201096663Y (en) | 2007-06-27 | 2007-06-27 | High-pressure dust-containing gas sampling pressure-reducing device |
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| Publication Number | Publication Date |
|---|---|
| CN201096663Y true CN201096663Y (en) | 2008-08-06 |
Family
ID=39923716
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|---|---|---|---|
| CNU2007201694424U Expired - Lifetime CN201096663Y (en) | 2007-06-27 | 2007-06-27 | High-pressure dust-containing gas sampling pressure-reducing device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101334343B (en) * | 2007-06-27 | 2011-02-09 | 中国石油天然气股份有限公司 | High-pressure dusty gas sampling and pressure reducing method and device |
| CN105486549A (en) * | 2016-01-20 | 2016-04-13 | 四川大学 | Sampling system capable of realizing constant-flow isokinetic sampling |
| CN110894777A (en) * | 2018-09-07 | 2020-03-20 | 中国石油化工股份有限公司 | Sampling device and method for movable wellhead |
-
2007
- 2007-06-27 CN CNU2007201694424U patent/CN201096663Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101334343B (en) * | 2007-06-27 | 2011-02-09 | 中国石油天然气股份有限公司 | High-pressure dusty gas sampling and pressure reducing method and device |
| CN105486549A (en) * | 2016-01-20 | 2016-04-13 | 四川大学 | Sampling system capable of realizing constant-flow isokinetic sampling |
| CN105486549B (en) * | 2016-01-20 | 2018-08-03 | 四川大学 | A kind of sampling system that can realize constant flow isokinetic sampling |
| CN110894777A (en) * | 2018-09-07 | 2020-03-20 | 中国石油化工股份有限公司 | Sampling device and method for movable wellhead |
| CN110894777B (en) * | 2018-09-07 | 2023-09-05 | 中国石油化工股份有限公司 | Sampling device and method for movable wellhead |
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