CN108079732A - Horizontal multi-stage separator - Google Patents
Horizontal multi-stage separator Download PDFInfo
- Publication number
- CN108079732A CN108079732A CN201810126982.7A CN201810126982A CN108079732A CN 108079732 A CN108079732 A CN 108079732A CN 201810126982 A CN201810126982 A CN 201810126982A CN 108079732 A CN108079732 A CN 108079732A
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- Prior art keywords
- filtration unit
- cylinder
- filter core
- filter
- horizontal multi
- Prior art date
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 78
- 238000001914 filtration Methods 0.000 claims abstract description 68
- 239000003345 natural gas Substances 0.000 claims abstract description 39
- 239000007788 liquid Substances 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000006073 displacement reaction Methods 0.000 claims description 3
- 238000002955 isolation Methods 0.000 claims 1
- 239000012535 impurity Substances 0.000 abstract description 7
- 239000007789 gas Substances 0.000 description 16
- 241000239290 Araneae Species 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 229930195733 hydrocarbon Natural products 0.000 description 4
- 150000002430 hydrocarbons Chemical class 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000001727 in vivo Methods 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000001273 butane Substances 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000003317 industrial substance Substances 0.000 description 1
- 239000003915 liquefied petroleum gas Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- CCEKAJIANROZEO-UHFFFAOYSA-N sulfluramid Chemical group CCNS(=O)(=O)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)C(F)(F)F CCEKAJIANROZEO-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0002—Casings; Housings; Frame constructions
- B01D46/0012—In-line filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
- B01D46/103—Curved filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/10—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
- B01D46/12—Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces in multiple arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
-
- 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
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/54—Specific separation steps for separating fractions, components or impurities during preparation or upgrading of a fuel
- C10L2290/547—Filtration for separating fractions, components or impurities during preparation or upgrading of a fuel
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Geometry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The invention discloses a kind of horizontal multi-stage separators,Be intended to provide it is a kind of have can carry out multistage filtering,It is hardly damaged filter core,The horizontal multi-stage separator for the advantages of improving filter efficiency and filter effect,Its key points of the technical solution are that,By-pass filtration unit is equipped with successively from inlet tube to outlet direction in cylinder,Secondary filtration unit and three-stage filtration unit,Isolated between by-pass filtration unit and secondary filtration unit by installing plate,By-pass filtration unit includes filter core and several flow-guiding bars being circumferentially positioned at outside filter core for natural gas to be guided to filter core,It is additionally provided on installing plate and penetrates the diversion pipe that installing plate sets and connects secondary filtration unit,Filter core is set on diversion pipe,Natural gas can be filtered three times,The impurity in natural gas will not be made to filter core direct collision simultaneously,It cannot be easily caused the damage of filter core,Whole filter efficiency can also be improved,And the filter effect to natural gas.
Description
Technical field
The present invention relates to gas treatment equipment fields, and in particular to a kind of horizontal multi-stage separator.
Background technology
Natural gas refers to naturally contain the mixture of the hydro carbons and non-hydrocarbon gases in stratum.In petroleum geology,
It is often referred to casing-head gas and reservoir gas.It is formed based on hydro carbons, and contains non-hydrocarbon gas.Natural gas is contained in underground porous gap rock
In layer, including casing-head gas, reservoir gas, coal bed gas, gas of mud volcano and biology generation gas etc., also have on a small quantity for coal seam.It is excellent
Matter fuel and industrial chemicals.
Natural gas is mainly used for making fuel, can manufacture carbon black, chemicals and liquefied petroleum gas, by natural gas production
Propane, butane are the important source materials of modern industry.
In the gathering and transportation technology in natural gas production gas field, mined natural gas is usually with some liquid from gas well
Body and solid impurity, such as condensate, condensation water, water flooding and landwaste dust, it is necessary to carry out gas-liquid in well site and gas gathering station
（Gu）Separating treatment is separated them from natural gas.Therefore separator become natural gas production processing during
Key equipment, it is desirable that separator separates light component, water and the impurity in natural gas as far as possible, reduces and is flowed into subordinate
Journey avoids influencing normal production and safety.
At present, the Chinese patent of Publication No. CN104056503A discloses a kind of multipurpose horizontal natural gas separating and filtering
Device, it includes cylinder, blind plate, blind plate retaining mechanism, and latch plate sliding cavity, blind plate are formed back to the one side of separating and filtering chamber in blind plate
Retaining mechanism includes latch plate, center dish axle, spider, towing plate and spider operation handle, in spider back to the one of blind plate
Side fixed center disk casing, spider casing is vertical with spider, is set on wall body of the blind plate back to the one side of separating and filtering chamber
Cylinder pressure release response means are put, which is engaged with spider, in the circumferencial direction of blind plate mating interface
And cleaning hole is opened up corresponding to the position of blind plate lock slots, sealing screw is arranged in cleaning hole.
Although this multipurpose horizontal natural gas separator-filter can fast and easily implement blind plate lock slots clear
It is clean, but since natural gas is directly with filter core making contact, while need to control the ingress rate of natural gas, after practical for a long time
Filter core is easily damaged, reduces its compressive resistance and filter efficiency, reduces filter effect.
The content of the invention
The object of the present invention is to provide a kind of horizontal multi-stage separators, and multistage filtering can be carried out by having, and be hardly damaged
The advantages of filter core, raising filter efficiency and filter effect.
The present invention above-mentioned technical purpose technical scheme is that：
A kind of horizontal multi-stage separator, the end socket including cylinder and arranged on cylinder both ends, cylinder both sides be respectively equipped with inlet tube and
Outlet, cylinder is interior to be equipped with by-pass filtration unit, secondary filtration unit and three-stage filtration successively from inlet tube to outlet direction
Unit is isolated between by-pass filtration unit and secondary filtration unit by installing plate, if by-pass filtration unit include filter core and
Dry root is circumferentially positioned at outside filter core for the flow-guiding bar for guiding natural gas to filter core, is additionally provided on installing plate and is penetrated installing plate and set
It puts and connects the diversion pipe of secondary filtration unit, filter core is set on diversion pipe.
By using above-mentioned technical proposal, natural gas enters from inlet tube in separator, and passes sequentially through by-pass filtration list
Member, secondary filtration unit and three-stage filtration unit are filtered, and in by-pass filtration unit, natural gas encounters flow-guiding bar and forms one
Grade filtering, makes big impurity particle be separated under collision, also avoids natural gas and directly generates collision to filter core；Flow-guiding bar is by day
Right gas is drained to filter core position, completes filtering, then enters secondary filtration unit by diversion pipe.
Natural gas can so be filtered three times, while impurity in natural gas will not be made to filter core direct collision,
It cannot be easily caused the damage of filter core, additionally it is possible to improve whole filter efficiency and the filter effect to natural gas.
Further set：Filter core is set in truncated conical shape, and the one end being relatively large in diameter is set on diversion pipe.
By using above-mentioned technical proposal, air-flow can be drained on the smaller one end of filter core diameter by flow-guiding bar, be passed through
The filtering of filter core, then by natural gas discharge to diversion pipe, make it into secondary filtration unit.Natural gas can be shunted, made
It is preferably filtered.
Further set：Secondary filtration unit includes being arranged on the in vivo wire mesh demister of cylinder, and wire mesh demister is in disk form
Shape, diameter are identical with the internal diameter of cylinder.
By using above-mentioned technical proposal, wire mesh demister can pool together the liquid in natural gas, and pass through
Drain pipe on cylinder outwards discharges, and improves whole filter effect.
Further set：Tertiary filter includes the filter plate arranged on outlet position, and filter plate is arc-shaped shape setting, and card is set
Below outlet, and it is embedded on cylinder inboard wall.
By using above-mentioned technical proposal, the setting of filter plate can achieve the effect that three-stage filtration, be embedded on inner wall
Replacement of the personnel to filter plate can be conveniently operated, improves the filter effect of whole service life and entirety.
Further set：Cylinder is outer to be equipped with liquid trap towards ground one side, and drain pipe, by-pass filtration are communicated on liquid trap
Unit, secondary filtration unit are equipped with the delivery pipe for connecting liquid trap with the cylinder body bottom of three-stage filtration cell position.
By using above-mentioned technical proposal, the liquid of filtering gained can be discharged into liquid trap by delivery pipe and deposit in natural gas
It stores up and passes through drain line drains, personnel easy to operation discharge the in vivo sewage of cylinder.
Further set：Outlet is equipped with pressure gauge connection.
Further set：Inlet tube is located on cylinder towards the position of diversion pipe, and flow-stopping plate, baffle are fixed on diversion pipe
Plate corresponds to inlet tube setting.
By using above-mentioned technical proposal, the setting of flow-stopping plate can stop inlet tube, avoid air-flow direct to pipeline
It is impacted, the service life of pipeline can be extended, so as to improve filter effect.
Further set：Displacement pipe is communicated on the cylinder of by-pass filtration cell position, cylinder is by being arranged on the saddle of its bottom
Seat supports.
By using above-mentioned technical proposal, cylinder can tively firm be supported by saddle, by replacing setting for pipe
It puts personnel easy to operation and cleans cylinder.
In conclusion the invention has the advantages that：
Natural gas can be filtered three times, while the impurity in natural gas will not be made to filter core direct collision, it is not easy to be made
Into the damage of filter core, additionally it is possible to improve whole filter efficiency and the filter effect to natural gas.
Description of the drawings
The present invention is further described below in conjunction with the accompanying drawings.
Fig. 1 is the structure diagram of embodiment 1.
In figure, 1, cylinder；11st, end socket；12nd, inlet tube；13rd, flow-stopping plate；14th, outlet；2nd, by-pass filtration unit；21、
Installing plate；22nd, filter core；23rd, flow-guiding bar；24th, diversion pipe；3rd, secondary filtration unit；31st, wire mesh demister；4th, three-stage filtration list
Member；41st, filter plate；5th, liquid trap；51st, drain pipe；52nd, delivery pipe；6th, pressure gauge connection；7th, displacement pipe；8th, saddle.
Specific embodiment
The specific embodiment of the present invention is described further below in conjunction with the accompanying drawings.
The technical solution adopted in the present invention is：
Embodiment 1, a kind of horizontal multi-stage separator, as shown in Figure 1, it includes generally cylindrical shape and in the cylinder of horizontal setting
Body 1,1 both ends of cylinder are fixed with end socket 11, and end socket 11 is set in semiellipse shape.1 bottom of cylinder is equipped with saddle 8, is used to support whole
A cylinder 1, the side wall in the front of cylinder 1 are equipped with inlet tube 12, and 1 top sidewall of cylinder is equipped with outlet 14, natural gas from into
Mouth pipe 12 enters and is discharged from outlet 14.
As shown in Figure 1, by-pass filtration unit 2, two level mistake are equipped with successively from inlet tube 12 to 14 direction of outlet in cylinder 1
Unit 3 and three-stage filtration unit 4 are filtered, is isolated between by-pass filtration unit 2 and secondary filtration unit 3 by installing plate 21.Level-one
Filter element 2 includes filter core 22, and filter core 22 extends to the left.22 right side of filter core is equipped with diversion pipe 24,24 saturating installing plate 21 of diversion pipe
It sets and connects secondary filtration unit 3.
It is circumferentially positioned at outside filter core 22 and is used for natural gas to filter as shown in Figure 1, by-pass filtration unit 2 further includes several
The flow-guiding bar 23 that core 22 guides, flow-guiding bar 23 are arranged on that filter core 22 is outer and 22 centre position of filter core, and filter core 22 is whole in coniform,
Its one end being relatively large in diameter is set on diversion pipe 24, and flow-guiding bar 23 is set around filter core 22, can gas be drained to filter core
22 positions are filtered.Inlet tube 12 is located on cylinder 1 towards the position of diversion pipe 24, and flow-stopping plate is fixed on diversion pipe 24
13, flow-stopping plate 13 corresponds to inlet tube 12 and sets, and air-flow can be avoided directly to impact diversion pipe 24.
As shown in Figure 1, secondary filtration unit 3 includes the wire mesh demister 31 being arranged in cylinder 1, wire mesh demister 31 is in circle
Disk shape, diameter is identical with the internal diameter of cylinder 1, and is embedded on 1 inner wall of cylinder.Diversion pipe 24 is set towards wire mesh demister 31
It puts, the natural gas after by-pass filtration can be drained on wire mesh demister 31 and carry out secondary filtration, by the liquid in natural gas
Separation.
As shown in Figure 1, tertiary filter includes the filter plate 41 arranged on 14 position of outlet, filter plate 41 is arc-shaped shape and sets
It puts, is fastened on 14 lower section of outlet, and is embedded on 1 inner wall of cylinder.Natural gas after secondary filtration passes through filter plate 41 simultaneously
It is discharged to 14 direction of outlet, since filter plate 41 is embedded on 1 inner wall of cylinder, radian is identical with 1 inner wall radian of cylinder, therefore
Operating personnel more conveniently can replace it after opening end socket 11.
As shown in Figure 1, cylinder 1 is outer to be equipped with liquid trap 5 towards ground one side, drain pipe 51, level-one are communicated on liquid trap 5
Filter element 2, secondary filtration unit 3 are equipped with the discharge for connecting liquid trap 5 with 1 bottom of cylinder of 4 position of three-stage filtration unit
Pipe 52, delivery pipe 52 is located on 1 side wall of cylinder of inlet tube 12 respectively, the cylinder 1 between installing plate 21 and wire mesh demister 31
On side wall and on 1 side wall of cylinder on 31 right side of wire mesh demister.Outlet 14 is equipped with pressure gauge connection 6, for detecting cylinder
Air pressure in body 1.
Natural gas enters from inlet tube 12 in separator, and passes sequentially through by-pass filtration unit 2,3 and of secondary filtration unit
Three-stage filtration unit 4 is filtered, and in by-pass filtration unit 2, natural gas encounters flow-guiding bar 23 and forms by-pass filtration, makes big
Impurity particle separates under collision；The liquid in gas can be separated in secondary filtration and three-stage filtration, and pass through discharge
Pipe 52 is discharged.
The above are preferred embodiments of the present invention, not makees limitation in any form, every foundation to the present invention
The technical spirit of the present invention belongs to inventive technique to any simple modification, equivalent change and modification made for any of the above embodiments
In the range of scheme.
Claims (8)
1. a kind of horizontal multi-stage separator, including horizontal cylinder（1）With arranged on cylinder（1）The end socket at both ends（11）, cylinder（1）
Both sides are respectively equipped with inlet tube（12）And outlet（14）, it is characterised in that：The cylinder（1）It is interior from inlet tube（12）To outlet
Pipe（14）Direction is equipped with by-pass filtration unit successively（2）, secondary filtration unit（3）With three-stage filtration unit（4）, by-pass filtration list
Member（2）With secondary filtration unit（3）Between pass through installing plate（21）Isolation, by-pass filtration unit（2）Including filter core（22）And
Several are circumferentially positioned at filter core（22）It is outer to be used for natural gas to filter core（22）The flow-guiding bar of guiding（23）, installing plate（21）On
It is additionally provided with and penetrates installing plate（21）It sets and connects secondary filtration unit（3）Diversion pipe（24）, filter core（22）It is set in water conservancy diversion
Pipe（24）On.
2. horizontal multi-stage separator according to claim 1, it is characterised in that：The filter core（22）It is set in truncated conical shape
It puts, the one end being relatively large in diameter is set in diversion pipe（24）On.
3. horizontal multi-stage separator according to claim 1, it is characterised in that：The secondary filtration unit（3）Including setting
In cylinder（1）Interior wire mesh demister（31）, wire mesh demister（31）Shape in disk form, diameter and cylinder（1）Internal diameter phase
Together.
4. horizontal multi-stage separator according to claim 1, it is characterised in that：The tertiary filter includes being arranged on outlet
Pipe（14）The filter plate of position（41）, filter plate（41）Shape setting is arc-shaped, is fastened on outlet（14）Lower section, and be embedded in cylinder
（1）On inner wall.
5. horizontal multi-stage separator according to claim 1, it is characterised in that：The cylinder（1）It is outer towards ground one side
Equipped with liquid trap（5）, liquid trap（5）On be communicated with drain pipe（51）, by-pass filtration unit（2）, secondary filtration unit（3）With three
Grade filter element（4）The cylinder of position（1）Bottom is equipped with connection liquid trap（5）Delivery pipe（52）.
6. horizontal multi-stage separator according to claim 5, it is characterised in that：The outlet（14）It is equipped with pressure gauge
Interface（6）.
7. horizontal multi-stage separator according to claim 1, it is characterised in that：The inlet tube（12）Positioned at cylinder（1）
On towards diversion pipe（24）Position, diversion pipe（24）On be fixed with flow-stopping plate（13）, flow-stopping plate（13）Corresponding inlet tube（12）
It sets.
8. horizontal multi-stage separator according to claim 7, it is characterised in that：The by-pass filtration unit（2）Position
Cylinder（1）On be communicated with displacement pipe（7）, cylinder（1）By the saddle for being arranged on its bottom（8）Support.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810126982.7A CN108079732A (en) | 2018-02-08 | 2018-02-08 | Horizontal multi-stage separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810126982.7A CN108079732A (en) | 2018-02-08 | 2018-02-08 | Horizontal multi-stage separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108079732A true CN108079732A (en) | 2018-05-29 |
Family
ID=62194448
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810126982.7A Withdrawn CN108079732A (en) | 2018-02-08 | 2018-02-08 | Horizontal multi-stage separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108079732A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110152435A (en) * | 2019-06-24 | 2019-08-23 | 浙江飞旋科技有限公司 | A kind of steam-water separator of magnetic suspension turbine vacuum pump |
| CN110252071A (en) * | 2019-07-22 | 2019-09-20 | 安徽扬天金塑新能源装备股份公司 | A kind of Horizontal gas filter separator |
| CN112029550A (en) * | 2019-09-09 | 2020-12-04 | 邵峥业 | Natural gas purifying and dehydrating device |
| CN112275032A (en) * | 2019-07-24 | 2021-01-29 | 中国石油天然气股份有限公司 | Horizontal filtering separator of gas transmission field |
| CN112280606A (en) * | 2020-12-29 | 2021-01-29 | 四川凌耘建科技有限公司 | Horizontal separation metering sledge and separation metering method thereof |
| CN113304564A (en) * | 2020-02-26 | 2021-08-27 | 绍兴广通节能环保科技有限公司 | Steam purification recovery unit |
| CN114452727A (en) * | 2021-12-15 | 2022-05-10 | 中国石油化工股份有限公司 | Purification liquid separation equipment |
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| CN110152435A (en) * | 2019-06-24 | 2019-08-23 | 浙江飞旋科技有限公司 | A kind of steam-water separator of magnetic suspension turbine vacuum pump |
| CN110252071A (en) * | 2019-07-22 | 2019-09-20 | 安徽扬天金塑新能源装备股份公司 | A kind of Horizontal gas filter separator |
| CN112275032A (en) * | 2019-07-24 | 2021-01-29 | 中国石油天然气股份有限公司 | Horizontal filtering separator of gas transmission field |
| CN112275032B (en) * | 2019-07-24 | 2022-06-03 | 中国石油天然气股份有限公司 | Horizontal filtering separator of gas transmission field |
| CN112029550A (en) * | 2019-09-09 | 2020-12-04 | 邵峥业 | Natural gas purifying and dehydrating device |
| CN112029550B (en) * | 2019-09-09 | 2022-02-01 | 徐倩倩 | Natural gas purifying and dehydrating device |
| CN113304564A (en) * | 2020-02-26 | 2021-08-27 | 绍兴广通节能环保科技有限公司 | Steam purification recovery unit |
| CN112280606A (en) * | 2020-12-29 | 2021-01-29 | 四川凌耘建科技有限公司 | Horizontal separation metering sledge and separation metering method thereof |
| CN114452727A (en) * | 2021-12-15 | 2022-05-10 | 中国石油化工股份有限公司 | Purification liquid separation equipment |
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Application publication date: 20180529 |