CN108219882A - The analysis anti-sulphur of sulphur well head blocks up system - Google Patents
The analysis anti-sulphur of sulphur well head blocks up system Download PDFInfo
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- CN108219882A CN108219882A CN201711191926.3A CN201711191926A CN108219882A CN 108219882 A CN108219882 A CN 108219882A CN 201711191926 A CN201711191926 A CN 201711191926A CN 108219882 A CN108219882 A CN 108219882A
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- Prior art keywords
- liquid
- separation device
- gas
- sulphur
- drusen
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- 239000005864 Sulphur Substances 0.000 title claims abstract description 89
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 238000004458 analytical method Methods 0.000 title claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 192
- 238000000926 separation method Methods 0.000 claims abstract description 135
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 72
- 239000002270 dispersing agent Substances 0.000 claims abstract description 42
- 239000003345 natural gas Substances 0.000 claims abstract description 36
- 241000191291 Abies alba Species 0.000 claims abstract description 31
- 239000007789 gas Substances 0.000 claims description 37
- 239000007787 solid Substances 0.000 claims description 16
- 238000011084 recovery Methods 0.000 claims description 13
- 230000000903 blocking effect Effects 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 6
- 238000004220 aggregation Methods 0.000 abstract description 3
- 230000002776 aggregation Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 14
- 239000011593 sulfur Substances 0.000 description 8
- 229910052717 sulfur Inorganic materials 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 6
- 230000008030 elimination Effects 0.000 description 4
- 238000003379 elimination reaction Methods 0.000 description 4
- 239000000243 solution Substances 0.000 description 3
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
- C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
- C10L3/10—Working-up natural gas or synthetic natural gas
- C10L3/101—Removal of contaminants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C9/00—Combinations with other devices, e.g. fans, expansion chambers, diffusors, water locks
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Cyclones (AREA)
Abstract
The present invention provides a kind of analysis anti-sulphur of sulphur well head to block up system, including：Christmas tree, throttle valve, dispersant add in device, Gas-liquid hydrocyclone separation device and liquid and consolidate cyclone separation device.Dispersant adds in device and sulphur removal aqueous dispersant is added between christmas tree and throttle valve, sulphur removal dispersant can reduce drusen surface tension and drusen is made to be distributed in water, it avoids drusen aggregation while also adds the drusen stably dispersing time, sulphur, which occurs, in throttle valve inlet after being depressured so as to avoid throttle valve blocks up phenomenon.Sulphur removal aqueous dispersant passes through after being mixed between christmas tree and throttle valve with the natural gas containing drusen to be entered by throttle valve in Gas-liquid hydrocyclone separation device, Gas-liquid hydrocyclone separation device detaches the natural gas of different densities and liquid, and scattered drusen includes in a liquid and then consolidates cyclone separation device by liquid and isolates drusen, it greatly strengthens separating effect, improve separative efficiency, contribute to the conveying of natural gas.
Description
Technical field
The present invention relates to the anti-sulphur plugging technique fields of well head more particularly to a kind of analysis anti-sulphur of sulphur well head to block up system.
Background technology
At present, after the natural gas both at home and abroad in high sulfur-bearing gas recovery well is produced via christmas tree, often in conveying natural gas
Sulphur depositional phenomenon occurs in surface gathering and transferring pipeline and corresponding processing unit, so as to be easy to occur sulfur plug gathering line, section
Situations such as flowing valve, separator, directly influences the normal production of gas recovery well.
In order to solve the problems, such as above-mentioned sulfur plug, common method has at this stage：The stifled method of steam coach pyrolysis, high pressure gas are blown
Sweep method, sulphur solvent soaking method, sulfur elimination annotation method etc..Wherein, the stifled method of steam coach pyrolysis primarily directed to tamper it is smaller, block
The lighter pipeline of situation, heats block part using steam coach and is melted tamper, and plugging removal effect is preferable, but
Corrosion easily is generated to pipeline, equipment, especially temperature is relatively low in winter, and effect is undesirable under the larger environment of humidity.High pressure gas
Sweeping method has to stop production to gas recovery well, and blocking position is purged using the high pressure gas at blocking position rear portion, then
Coordinating with steam rapid heat cycle vehicle blows out the foreign matter of blocking position, time-consuming longer, ineffective.Sulphur solvent soaking method mainly for it is small-sized can
The equipment of dismounting carries out mechanical cleaning and immersion, can not be suitable for gathering line and large scale equipment device, while also need to gas production
Well stops production, and practicability is not strong.Although the sulfur elimination annotation method studies in China time is later, just began one's study, removed in recent years
The shortcomings that application of sulphur agent filling technique compensates for above-mentioned several method, for different choking portions under the premise of production is not influenced
Position carries out effective de-plugging, and the scope of application is wider, influences the advantages that little to system production operating parameter, so being still main sulphur removal
Blocking method, but sulfur elimination has certain corrosivity and toxicity, while with penetrating odor, has secondary pollution to environment, and existing
The sulfur elimination Sulfur capacity in stage is low, and the reaction time is long, and simple substance sulphur could effectively be dissolved by needing to contact for a long time, increase additive amount
With the addition period.
Invention content
In view of the problem of background technology, the purpose of the present invention is to provide a kind of analysis anti-sulphur of sulphur well head to block up system,
It is disperseed by adding sulphur removal aqueous dispersant in throttle valve upstream with that will contain the drusen in the natural gas of drusen
It opens, avoids at throttle valve and sulphur occur and block up phenomenon；It by Gas-liquid hydrocyclone separation device and liquid also by consolidating cyclone separation device
It is applied in combination, the natural gas containing drusen and the gas, liquid, solid in the mixture of sulphur removal aqueous dispersant is effectively divided
From enhancing separating effect, improve separative efficiency, contribute to the conveying of natural gas.
To achieve these goals, the present invention provides a kind of analysis anti-sulphur of sulphur well head to block up system, including：Christmas tree, section
Stream valve, dispersant add in device, Gas-liquid hydrocyclone separation device and liquid and consolidate cyclone separation device.
Christmas tree is communicated in gas recovery well and produces the natural gas containing drusen in gas recovery well.
Throttle valve is set to the downstream of christmas tree and is communicated in christmas tree, and with throttling valve inlet and throttling valve outlet.
Dispersant adds in device and contains sulphur removal aqueous dispersant, is set between christmas tree and throttle valve and is communicated in section
Flow valve inlet.
Gas-liquid hydrocyclone separation device is set to the downstream of throttle valve, and has：Gas-liquid hydrocyclone separation device entrance, is communicated in
Throttle valve outlet；Gas-liquid hydrocyclone separation device gas vent；And Gas-liquid hydrocyclone separation device liquid outlet.
Liquid consolidates cyclone separation device and is set to the downstream of Gas-liquid hydrocyclone separation device, and have：Liquid consolidates cyclone separation device
Entrance is communicated in Gas-liquid hydrocyclone separation device liquid outlet；Liquid consolidates cyclone separation device liquid outlet；And liquid consolidates cyclonic separation
Device solid outlet.
Wherein, dispersant adds in device and adds in sulphur removal aqueous dispersant between christmas tree and throttle valve, in gas recovery well
After natural gas containing drusen is produced via christmas tree, it is dispersed under the action of sulphur removal aqueous dispersant and via section
Flow valve, Gas-liquid hydrocyclone separation device entrance is flowed into Gas-liquid hydrocyclone separation device.
In Gas-liquid hydrocyclone separation device, Gas-liquid hydrocyclone separation device is to sulphur removal aqueous dispersant and containing drusen
The mixture of natural gas carries out gas-liquid separation, and the natural gas isolated is discharged via Gas-liquid hydrocyclone separation device gas vent, and
The liquid containing drusen isolated is consolidated cyclone separation device entrance via Gas-liquid hydrocyclone separation device liquid outlet, liquid and is flowed into
Liquid is consolidated in cyclone separation device.
To consolidate in cyclone separation device in liquid, liquid consolidates cyclone separation device and carries out solid-liquor separation to the liquid containing drusen,
The liquid isolated consolidates the discharge of cyclone separation device liquid outlet via liquid, and the drusen isolated consolidates eddy flow point via liquid
It is discharged from device solid outlet.
Beneficial effects of the present invention are as follows：
Blocked up in system in the analysis anti-sulphur of sulphur well head according to the present invention, by dispersant add in device christmas tree and throttle valve it
Between add in sulphur removal aqueous dispersant, the wherein sulphur removal dispersant in sulphur removal aqueous dispersant can reduce drusen surface
Tension simultaneously makes drusen be distributed in water, when avoiding drusen aggregation while also adding drusen stably dispersing
Between, sulphur occurs in throttle valve inlet after being depressured so as to avoid throttle valve and blocks up phenomenon.Also, sulphur removal aqueous dispersant is with containing
The natural gas of drusen enters Gas-liquid hydrocyclone separation device via throttle valve together after being mixed between christmas tree and throttle valve
In, Gas-liquid hydrocyclone separation device is detached the natural gas of different densities and liquid by cyclonic action, and scattered sulphur
Grain comprising in a liquid and then consolidating cyclone separation device by liquid and isolate drusen, so as to greatly strengthen separating effect,
Separative efficiency is improved, and then contributes to the conveying of natural gas.In addition, Gas-liquid hydrocyclone separation device and liquid consolidate cyclone separation device
Can be achieved miniaturization, skid, can directly entrucking roping, reduce installation workload, and may be reused.
Description of the drawings
Fig. 1 is the process flow diagram that the analysis anti-sulphur of sulphur well head according to the present invention blocks up system.
Wherein, the reference numerals are as follows：
1 christmas tree, 5 liquid consolidates cyclone separation device
2 throttle valve, 51 liquid consolidates cyclone separation device entrance
21 throttling 52 liquid of valve inlet consolidate cyclone separation device liquid outlet
22 throttling 53 liquid of valve outlet consolidate cyclone separation device solid outlet
3 dispersants add in 6 gas reception device of device
4 Gas-liquid hydrocyclone separation device, 7 Liquid acquisition device
41 Gas-liquid hydrocyclone separation device entrance, 8 solid reception device
42 Gas-liquid hydrocyclone separation device gas vent A gas recovery wells
43 Gas-liquid hydrocyclone separation device liquid outlets
Specific embodiment
With reference to the accompanying drawings system is blocked up the analysis anti-sulphur of sulphur well head according to the present invention is described in detail.
With reference to Fig. 1, the analysis anti-sulphur system of blocking up of sulphur well head according to the present invention includes：Christmas tree 1, throttle valve 2, dispersant add in
Device 3, Gas-liquid hydrocyclone separation device 4 and liquid consolidate cyclone separation device 5.
Christmas tree 1 is communicated in gas recovery well A and produces the natural gas containing drusen in gas recovery well A.Throttle valve 2 is set to
The downstream of christmas tree 1 is simultaneously communicated in christmas tree 1, and with throttling valve inlet 21 and throttling valve outlet 22.
Dispersant adds in device 3 and contains sulphur removal aqueous dispersant, is set between christmas tree 1 and throttle valve 2 and connects
In throttling valve inlet 21.
Gas-liquid hydrocyclone separation device 4 is set to the downstream of throttle valve 2, and has：Gas-liquid hydrocyclone separation device entrance 41, even
Pass through throttling valve outlet 22；Gas-liquid hydrocyclone separation device gas vent 42；And Gas-liquid hydrocyclone separation device liquid outlet 43.
Liquid consolidates cyclone separation device 5 and is set to the downstream of Gas-liquid hydrocyclone separation device 4, and have：Liquid consolidates cyclonic separation dress
Posting port 51 is communicated in Gas-liquid hydrocyclone separation device liquid outlet 43；Liquid consolidates cyclone separation device liquid outlet 52；And liquid is consolidated
Cyclone separation device solid outlet 53.
Wherein, dispersant adds in device 3 and sulphur removal aqueous dispersant is added between christmas tree 1 and throttle valve 2 (i.e. except sulphur content
Powder is dissolved into the solution formed in water), after the natural gas containing drusen in gas recovery well A is produced via christmas tree 1, except
It is dispersed under the action of sulphur aqueous dispersant and flows into gas-liquid rotation via throttle valve 2, Gas-liquid hydrocyclone separation device entrance 41
In flow splitting device 4.
In Gas-liquid hydrocyclone separation device 4, Gas-liquid hydrocyclone separation device 4 is to sulphur removal aqueous dispersant with containing drusen
Natural gas mixture carry out gas-liquid separation, the natural gas isolated is via 42 row of Gas-liquid hydrocyclone separation device gas vent
Go out, and the liquid containing drusen isolated consolidates cyclone separation device via Gas-liquid hydrocyclone separation device liquid outlet 43, liquid
51 influent of entrance is consolidated in cyclone separation device 5.
Consolidate in cyclone separation device 5 in liquid, liquid consolidates cyclone separation device 5 and the liquid progress liquid containing drusen is divided admittedly
From the liquid isolated is consolidated cyclone separation device liquid outlet 52 via liquid and discharged, and the drusen isolated is consolidated via liquid
Cyclone separation device solid outlet 53 is discharged.
It is blocked up in system in the analysis anti-sulphur of sulphur well head according to the present invention, device 3 is added in christmas tree 1 and throttle valve by dispersant
Sulphur removal aqueous dispersant is added between 2, the wherein sulphur removal dispersant in sulphur removal aqueous dispersant can reduce drusen
Surface tension simultaneously makes drusen be distributed in water, avoids drusen aggregation while also adds drusen dispersion surely
It fixes time, sulphur, which occurs, at throttling valve inlet 21 after being depressured so as to avoid throttle valve 2 blocks up phenomenon.Also, sulphur removal dispersant water
Solution enters gas-liquid via throttle valve 2 together after being mixed between christmas tree 1 and throttle valve 2 with the natural gas containing drusen and revolves
In flow splitting device 4, Gas-liquid hydrocyclone separation device 4 is detached the natural gas of different densities and liquid by cyclonic action, and is divided
The drusen to scatter, which includes in a liquid and then consolidates cyclone separation device 5 by liquid, isolates drusen, so as to increase
Strong separating effect improves separative efficiency, and then contribute to the conveying of natural gas.In addition, Gas-liquid hydrocyclone separation device 4 and liquid
Gu cyclone separation device 5 can realize miniaturization, skid, can directly entrucking roping, reduce installation workload, and can weigh
It is multiple to use.
Dispersant, which adds in device 3, to be a kind of pipeline pump, and pipeline pump is between christmas tree 1 and throttle valve 2 to containing drusen
Natural gas in add in sulphur removal aqueous dispersant.Wherein, sulphur removal aqueous dispersant can be sodium dodecyl sulfate aqueous solution,
I.e. dodecyl sodium sulfate is dissolved into the solution formed in water.
With reference to Fig. 1, Gas-liquid hydrocyclone separation device gas vent 42 can be located at the top of Gas-liquid hydrocyclone separation device 4, and gas
Liquid cyclone separation device liquid outlet 43 is located at the bottom of Gas-liquid hydrocyclone separation device 4.Gas-liquid hydrocyclone separation device gas vent
42 with the position relationship in this structure of Gas-liquid hydrocyclone separation device liquid outlet 43, convenient for natural gas and containing drusen
Liquid is discharged from Gas-liquid hydrocyclone separation device 4 respectively.With reference to Fig. 1, liquid, which consolidates cyclone separation device liquid outlet 52, can be located at liquid
Though the top of cyclone separation device 5, liquid consolidates cyclone separation device solid outlet 53 and is located at the bottom that liquid consolidates cyclone separation device 5
Portion.Liquid consolidates cyclone separation device liquid outlet 52 and consolidates the pass of the position in this structure of cyclone separation device solid outlet 53 with liquid
System, consolidates in cyclone separation device 5 respectively from liquid convenient for liquid and drusen and discharges.
With reference to Fig. 1, the analysis anti-sulphur system of blocking up of sulphur well head may also include：Gas reception device 6 is communicated in gas-liquid cyclonic separation dress
Gas vent 42 is put to receive the natural gas that Gas-liquid hydrocyclone separation device 4 is isolated.Gas reception device 6 can be it is any can be right
The device that natural gas is further processed.
With reference to Fig. 1, the analysis anti-sulphur system of blocking up of sulphur well head may also include：Liquid acquisition device 7 is communicated in liquid and consolidates cyclonic separation dress
It puts liquid outlet 52 and the liquid that cyclone separation device 5 isolates is consolidated with receiving liquid.Liquid acquisition device 7 can be it is any can be to liquid
Gu the device that the liquid that cyclone separation device 5 is isolated is further processed.With reference to Fig. 1, the analysis anti-sulphur of sulphur well head blocks up system also
It may include：Solid reception device 8 is communicated in liquid and consolidates cyclone separation device solid outlet 53 and consolidates cyclone separation device 5 with receiving liquid
The drusen isolated.Liquid, which consolidates the drusen that cyclone separation device 5 is isolated, to be comprehensively utilized.
It finally remarks additionally, christmas tree 1, throttle valve 2, Gas-liquid hydrocyclone separation device 4 and liquid consolidate cyclonic separation dress
It is connected between putting 5 by corresponding connecting pipeline, gas reception device 6 is communicated in gas-liquid cyclonic separation by natural gas line
Device gas vent 42, Liquid acquisition device 7 are communicated in liquid by blowdown pipeline and consolidate cyclone separation device liquid outlet 52, own
Connecting pipeline, natural gas line and blowdown pipeline form together conveying natural gas surface gathering and transferring pipeline.The present invention is defeated
During sending the natural gas containing drusen, device 3, Gas-liquid hydrocyclone separation device 4 and liquid are added in based on dispersant and consolidate eddy flow point
Collective effect from device 5, additionally it is possible to it avoids any position of the drusen in surface gathering and transferring pipeline that sulphur occurs and blocks up phenomenon, from
And contribute to the conveying of natural gas.
Claims (6)
1. a kind of analysis anti-sulphur of sulphur well head blocks up system, including：
Christmas tree (1) is communicated in gas recovery well (A) and produces the natural gas containing drusen in gas recovery well (A)；
Throttle valve (2) is set to the downstream of christmas tree (1) and is communicated in christmas tree (1), has throttling valve inlet (21) and throttling
Valve outlet (22)；
It is characterized in that, the analysis anti-sulphur system of blocking up of sulphur well head further includes：
Dispersant adds in device (3), contains sulphur removal aqueous dispersant, is set between christmas tree (1) and throttle valve (2) and connects
Pass through throttling valve inlet (21)；
Gas-liquid hydrocyclone separation device (4), is set to the downstream of throttle valve (2), and has：
Gas-liquid hydrocyclone separation device entrance (41) is communicated in throttling valve outlet (22)；
Gas-liquid hydrocyclone separation device gas vent (42)；And
Gas-liquid hydrocyclone separation device liquid outlet (43)；
Liquid consolidates cyclone separation device (5), is set to the downstream of Gas-liquid hydrocyclone separation device (4), and has：
Liquid consolidates cyclone separation device entrance (51), is communicated in Gas-liquid hydrocyclone separation device liquid outlet (43)；
Liquid consolidates cyclone separation device liquid outlet (52)；
Liquid consolidates cyclone separation device solid outlet (53)；
Wherein, dispersant adds in device (3) and sulphur removal aqueous dispersant, gas recovery well is added between christmas tree (1) and throttle valve (2)
(A) after the natural gas containing drusen in is produced via christmas tree (1), disperseed under the action of sulphur removal aqueous dispersant
It opens and is flowed into Gas-liquid hydrocyclone separation device (4) via throttle valve (2), Gas-liquid hydrocyclone separation device entrance (41)；
In Gas-liquid hydrocyclone separation device (4), Gas-liquid hydrocyclone separation device (4) is to sulphur removal aqueous dispersant with containing drusen
Natural gas mixture carry out gas-liquid separation, the natural gas isolated via Gas-liquid hydrocyclone separation device gas vent (42) arrange
Go out, and the liquid containing drusen isolated is consolidated cyclonic separation via Gas-liquid hydrocyclone separation device liquid outlet (43), liquid and is filled
Posting port (51) influent is consolidated in cyclone separation device (5)；
Consolidate in cyclone separation device (5) in liquid, liquid consolidates cyclone separation device (5) and the liquid progress liquid containing drusen is divided admittedly
From the liquid isolated is consolidated cyclone separation device liquid outlet (52) via liquid and discharged, and the drusen isolated is via liquid
Gu cyclone separation device solid outlet (53) is discharged.
2. the analysis anti-sulphur of sulphur well head according to claim 1 blocks up system, which is characterized in that Gas-liquid hydrocyclone separation device gas goes out
Mouth (42) is positioned at the top of Gas-liquid hydrocyclone separation device (4), and Gas-liquid hydrocyclone separation device liquid outlet (43) is revolved positioned at gas-liquid
The bottom of flow splitting device (4).
3. the analysis anti-sulphur of sulphur well head according to claim 1 blocks up system, which is characterized in that liquid consolidates cyclone separation device liquid discharge
Mouthful (52) consolidate the top of cyclone separation device (5) positioned at liquid, and liquid is consolidated cyclone separation device solid outlet (53) and revolved admittedly positioned at liquid
The bottom of flow splitting device (5).
4. the analysis anti-sulphur of sulphur well head according to claim 1 blocks up system, which is characterized in that the analysis anti-sulphur of sulphur well head blocks up system and also wraps
It includes：Gas reception device (6) is communicated in Gas-liquid hydrocyclone separation device gas vent (42) to receive Gas-liquid hydrocyclone separation device
(4) natural gas isolated.
5. the analysis anti-sulphur of sulphur well head according to claim 1 blocks up system, which is characterized in that the analysis anti-sulphur of sulphur well head blocks up system and also wraps
It includes：Liquid acquisition device (7) is communicated in liquid and consolidates cyclone separation device liquid outlet (52) and consolidates cyclone separation device with receiving liquid
(5) liquid isolated.
6. the analysis anti-sulphur of sulphur well head according to claim 1 blocks up system, which is characterized in that the analysis anti-sulphur of sulphur well head blocks up system and also wraps
It includes：Solid reception device (8) is communicated in liquid and consolidates cyclone separation device solid outlet (53) and consolidates cyclone separation device with receiving liquid
(5) drusen isolated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711191926.3A CN108219882B (en) | 2017-11-24 | 2017-11-24 | Sulfur-separating well head sulfur-blocking preventing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711191926.3A CN108219882B (en) | 2017-11-24 | 2017-11-24 | Sulfur-separating well head sulfur-blocking preventing system |
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| CN108219882A true CN108219882A (en) | 2018-06-29 |
| CN108219882B CN108219882B (en) | 2024-06-04 |
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| CN201711191926.3A Active CN108219882B (en) | 2017-11-24 | 2017-11-24 | Sulfur-separating well head sulfur-blocking preventing system |
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Cited By (4)
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|---|---|---|---|---|
| CN109135706A (en) * | 2018-08-30 | 2019-01-04 | 中石化节能环保工程科技有限公司 | A kind of sulphur dispersion stabilizer preventing analysis sulphur well head sulfur plug |
| CN110193239A (en) * | 2019-06-21 | 2019-09-03 | 巨涛油田服务(天津)有限公司 | It is a kind of for pressure liquid and solid removal technology |
| CN110452749A (en) * | 2019-06-21 | 2019-11-15 | 巨涛油田服务(天津)有限公司 | A kind of low resistance cyclonic well head high sulfur-containing natural gas purification method |
| CN113959894A (en) * | 2021-10-27 | 2022-01-21 | 中国石油天然气股份有限公司西南油气田分公司勘探开发研究院 | Method for measuring sulfur content in gas produced from sulfur-containing gas well |
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