CN204411986U - Combined separator - Google Patents
Combined separator Download PDFInfo
- Publication number
- CN204411986U CN204411986U CN201420783068.7U CN201420783068U CN204411986U CN 204411986 U CN204411986 U CN 204411986U CN 201420783068 U CN201420783068 U CN 201420783068U CN 204411986 U CN204411986 U CN 204411986U
- Authority
- CN
- China
- Prior art keywords
- housing
- baffle
- cyclone
- plate
- combined separator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
The utility model relates to a kind of Combined separator, comprise housing, housing is provided with air inlet pipe, gas outlet, primary cyclone is provided with successively from bottom to top in housing, secondary cyclone, mist eliminator, coarse separation filter core, air inlet pipe is communicated to primary cyclone, the upper end of primary cyclone is provided with the first baffle plate, hydrops room is formed between first baffle plate and housing bottom, hydrops room sidewall is provided with liquid level gauge, visor, row's bubble mouth, hydrops is provided with blow-off pipe bottom room, the top of secondary cyclone is provided with second baffle, second baffle is provided with the mozzle extending to hydrops room, the lower end of coarse separation filter core is provided with third gear plate, the upper side wall of third gear plate is provided with sewage draining exit, the madial wall of housing is provided with the deflection plate of corresponding gas outlet, the top of housing is provided with quick operating valve.This utility model dust removal rate is high, separation accuracy is high, be easy to observe internal state, blowdown row bubble rationally, stabilized structure, practical, easy to maintenance.
Description
Technical field
The utility model belongs to natural gas gas-liquid separation technical field, is specifically related to a kind of Combined separator.
Background technology
At petroleum chemical industry, gas-liquid separation is one of the important foundation process of material recycle, purification of products, gas-liquid separation realizes mainly through gas-liquid separator, because the natural gas exploited out from gas well contains the plurality of impurities such as solid particle, drop, " mist ", these impurity can produce significant impact to upstream device, have to pass through separating and filtering process, to reach the effect of udst separation.Because the physical attribute such as granular size of impurity various in natural gas is different, multiple separating component is adopted to be combined to form Combined separator, can the impurity of different physical attribute in divided gas flow, the parts composition of gas-liquid separator and structure thereof directly affect effect and the separation accuracy of separation, and existing Combined separator ubiquity is separated the problems such as progression is few, separative efficiency is low, separation accuracy is inadequate, maintenance is inconvenient.
Number of patent application be 201420000870.4 utility model patent disclose a kind of purified natural gas device, this device includes cyclone separator, mist extractor, coalescing separator, natural gas carries out one cyclonic separation through cyclone separator successively, mist extractor carries out catching mist, vane type coalescing separator carries out secondary coarse separation, the air inlet of this device only just enters mist extractor after one cyclonic is separated, separating effect is not good enough, superstructure is closed, inconvenient to the breakdown maintenance of coalescing separator, in air inlet containing foam discharging agent, bubble obviously in fluid collection chamber, even if bottom liquid is little, the alveolar layer of liquid level also can be accumulated rapidly, need continually bottom switch leakage fluid dram with in good time discharge opeing row bubble, therefore inefficiency.
Utility model content
For above-mentioned weak point of the prior art, the utility model aims to provide that a kind of separative efficiency is high, separation accuracy is high, blowdown row bubble is convenient, be convenient to observe internal state, compact conformation, Combined separator rationally distributed, easy to maintenance.
To achieve these goals, the technical solution of the utility model: a kind of Combined separator, comprise housing, described housing is provided with air inlet pipe, gas outlet, primary cyclone is provided with successively from bottom to top in described housing, secondary cyclone, mist eliminator, coarse separation filter core, described air inlet pipe is communicated to described primary cyclone, the upper end of described primary cyclone is provided with the first baffle plate, hydrops room is formed between described first baffle plate and described housing bottom, the sidewall of described hydrops room is provided with row's bubble mouth, visor, the top of described secondary cyclone is provided with second baffle, described second baffle is provided with the mozzle extending to described hydrops room, the lower end of described coarse separation filter core is provided with third gear plate, the upper side wall of described third gear plate is provided with sewage draining exit, the madial wall of described housing is provided with the deflection plate of corresponding described gas outlet, the top of described housing is provided with quick operating valve.
Further, the sidewall of described hydrops room is provided with liquid level gauge, is convenient to the aqueous condition of bubble of observing hydrops indoor.
Further, bottom described hydrops room, be provided with blow-off pipe, for discharging the liquid of hydrops indoor.
Further, the bottom of described primary cyclone and mozzle is all fixed on by support member on the madial wall of described housing, stabilized structure.
Further, the upper outlet of described secondary cyclone is higher than described second baffle, the lower end of described secondary cyclone extends to described hydrops room through described first baffle plate, ensure that being separated the liquid flowed out in coarse separation filter core enters hydrops room from mozzle, and secondary cyclone again can not be entered, the isolated liquid of secondary cyclone is to indoor downstream to hydrops simultaneously.
Further, described mist eliminator is vane type mist eliminator or wire-mesh mist extractor.
Further, described deflection plate cross section be polygon or circular arc.
Further, the inwall of described deflection plate and described housing forms upper opening, go to the bottom and close and correspond to the baffling cavity of described gas outlet, and the lower shoe of described deflection plate flushes with the downside of described gas outlet.
The beneficial effects of the utility model: the primary cyclone of this Combined separator has efficiently been separated solid particle polluter in gas and drop, in the main divided gas flow of secondary cyclone, particle diameter is at the impurity of about 10 μm, and in mist eliminator removing gas, particle diameter is at " mist " shape impurity of 3 ~ 5 μm, in the main divided gas flow of coarse separation filter core, particle diameter is at micro-impurity of about 0.5 μm, filtering accuracy is high, coalescent effective, flux density is large, separating rate is fast, contamination capacity is large, long service life, there is impurity screening, the dual-use function of coalescent moisture content, realize filtering the essence of gas, this utility model also realizes independent blowdown respectively, row's bubble, the aqueous condition of bubble that staff can be observed in housing by visor, be convenient to arrange bubble in good time, liquid level gauge shows the liquid level of hydrops indoor in real time, be convenient to discharge liquid in good time, internal liquid is avoided to accumulate excessive, the quick operating valve at top can high-speed switch, plant maintenance is convenient.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the A-A sectional view in Fig. 1;
In figure, 1, housing, 2, air inlet pipe, 3, primary cyclone, 4, secondary cyclone, 5, mist eliminator, 6, coarse separation filter core, 7, blow-off pipe, 8, liquid level gauge, 9, hydrops room, 10, support member, 11, row's bubble mouth, 12, visor, the 13, first baffle plate, 14, mozzle, 15, secondary cyclone separating chamber, 16, second baffle, 17, catch fog chamber, 18, third gear plate, 19, sewage draining exit, 20, coarse separation room, 21, gas outlet, 22, deflection plate, 23, quick operating valve.
Detailed description of the invention
The utility model is further described below in conjunction with specific embodiment and accompanying drawing.
A kind of Combined separator as depicted in figs. 1 and 2, comprise housing 1, housing 1 is provided with air inlet pipe 2, gas outlet 21, primary cyclone 3 is provided with successively from bottom to top in housing 1, secondary cyclone 4, mist eliminator 5, coarse separation filter core 6, mist eliminator 5 is vane type mist eliminator or wire-mesh mist extractor, air inlet pipe 2 is communicated to primary cyclone 3, the upper end of primary cyclone 3 is provided with the first baffle plate 13, hydrops room 9 is formed between bottom first baffle plate 13 and housing 1, the sidewall of hydrops room 9 is provided with liquid level gauge 8, row's bubble mouth 11, visor 12, liquid level gauge 8 can monitor the amount of liquid in display hydrops room 9, control its liquid level and remain on row's bubble mouth less than 11, visor 12 is for observing the inner aqueous condition of bubble, after alveolar layer reach a certain height, the row's of opening bubble mouth 11 carries out row's bubble, blow-off pipe 7 is provided with bottom hydrops room 9, in good time blowdown after liquid reach a certain height.The top of secondary cyclone 4 is provided with second baffle 16, second baffle 16 is provided with the mozzle 14 extending to hydrops room 9, the upper outlet of secondary cyclone 4 is higher than second baffle 16, the liquid on second baffle 16 is effectively avoided to flow in secondary cyclone, the lower end of secondary cyclone 4 extends to hydrops room 9 through the first baffle plate 13, the bottom of primary cyclone 3 and mozzle 14 is all fixed on by support member 10 on the madial wall of housing 1, stabilized structure.Secondary cyclone separating chamber 15 is formed between first baffle plate 13 and second baffle 16, the lower end of coarse separation filter core 6 is provided with third gear plate 18, third gear plate more than 18 is coarse separation room 20, the upper side wall of third gear plate 18 is provided with sewage draining exit 19, for catching fog chamber 17 between second baffle 16 and third gear plate 18, third gear plate more than 18 is coarse separation room 20, the madial wall of housing 1 is provided with the deflection plate 22 of corresponding gas outlet 21, deflection plate 22 cross section can be the various shape such as polygon or circular arc, deflection plate 22 forms upper opening with the inwall of housing 1, go to the bottom and close and correspond to the baffling cavity of gas outlet 21, the lower shoe of deflection plate 22 flushes with the downside of gas outlet 21.When the lower shoe collection of deflection plate 22 has liquid, liquid can flow out from exhaust outlet 21 with gas, can not remain in the bottom of baffling cavity.The top of housing 1 is provided with quick operating valve 23, is convenient to more renew cartridge and daily maintenance.
Natural gas in gas well enters primary cyclone 3 by air inlet pipe 2, solid particle in gas and large drop are separated through one cyclonic and flow into hydrops room 9, gas enters secondary cyclone separating chamber 15, in the main divided gas flow of secondary cyclone 4, particle diameter is at the impurity of about 10 μm, isolated impurity also flows into hydrops room 9, gas upwards enters catches fog chamber 17, mist eliminator 5 isolates particle diameter at the impurity of 3 ~ 5 μm, the liquid assembled flows into hydrops room 9 through mozzle 14, gas upwards enters coarse separation filter core 6, realize essence to filter, isolate micro-impurity of about 0.5 μm, coalescent moisture content simultaneously, the liquid of coarse separation filter core 6 inwall is successively through catching fog chamber 17, mozzle 14 flows into hydrops room 9, the liquid of coarse separation filter core 6 outer surface is because gravity is downstream to third gear plate 18, discharge through sewage draining exit 19, gas after essence filtration is successively by deflection plate 22, gas outlet 21 is flowed out, enter upstream device.Gas flows out coarse separation filter core 6 and enters in the process of deflection plate 22, and the liquid carried secretly in gas can because gravitational settling be to third gear plate 18, thus cutting out partial liquid further.
This Combined separator carries out one cyclonic separation, secondary cyclonic separation successively to air-flow, catches mist, coarse separation, baffling are given vent to anger, and dust removal rate is high, separation accuracy is high, and blowdown, row's bubble are convenient, are easy to observe inner bubble liquid situation, easy to maintenance.
Above the technical scheme that the utility model embodiment provides is described in detail, apply specific case herein to set forth the principle of the utility model embodiment and embodiment, the explanation of above embodiment is only applicable to the principle helping to understand the utility model embodiment; Meanwhile, for one of ordinary skill in the art, according to the utility model embodiment, detailed description of the invention and range of application all will change, and in sum, this description should not be construed as restriction of the present utility model.
Claims (8)
1. a Combined separator, comprise housing (1), described housing (1) is provided with air inlet pipe (2), gas outlet (21), it is characterized in that, primary cyclone (3) is provided with from bottom to top successively in described housing (1), secondary cyclone (4), mist eliminator (5), coarse separation filter core (6), described air inlet pipe (2) is communicated to described primary cyclone (3), the upper end of described primary cyclone (3) is provided with the first baffle plate (13), hydrops room (9) is formed between described first baffle plate (13) and described housing (1) bottom, the sidewall of described hydrops room (9) is provided with row's bubble mouth (11), visor (12), the top of described secondary cyclone (4) is provided with second baffle (16), described second baffle (16) is provided with the mozzle (14) extending to described hydrops room (9), the lower end of described coarse separation filter core (6) is provided with third gear plate (18), the upper side wall of described third gear plate (18) is provided with sewage draining exit (19), the madial wall of described housing (1) is provided with the deflection plate (22) of corresponding described gas outlet (21), the top of described housing (1) is provided with quick operating valve (23).
2. Combined separator as claimed in claim 1, it is characterized in that, the sidewall of described hydrops room (9) is provided with liquid level gauge (8).
3. Combined separator as claimed in claim 1, is characterized in that, described hydrops room (9) bottom is provided with blow-off pipe (7).
4. Combined separator as claimed in claim 1, it is characterized in that, the bottom of described primary cyclone (3) and mozzle (14) is all fixed on the madial wall of described housing (1) by support member (10).
5. Combined separator as claimed in claim 1, it is characterized in that, the upper outlet of described secondary cyclone (4) is higher than described second baffle (16), and the lower end of described secondary cyclone (4) extends to described hydrops room (9) through described first baffle plate (13).
6. Combined separator as claimed in claim 1, it is characterized in that, described mist eliminator (5) is vane type mist eliminator or wire-mesh mist extractor.
7. Combined separator as claimed in claim 1, is characterized in that, described deflection plate (22) cross section be polygon or circular arc.
8. Combined separator as claimed in claim 1, it is characterized in that, the inwall of described deflection plate (22) and described housing (1) forms upper opening, go to the bottom and to close and corresponding to the baffling cavity of described gas outlet (21), the lower shoe of described deflection plate (22) flushes with the downside of described gas outlet (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420783068.7U CN204411986U (en) | 2014-12-11 | 2014-12-11 | Combined separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420783068.7U CN204411986U (en) | 2014-12-11 | 2014-12-11 | Combined separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204411986U true CN204411986U (en) | 2015-06-24 |
Family
ID=53462396
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420783068.7U Expired - Fee Related CN204411986U (en) | 2014-12-11 | 2014-12-11 | Combined separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204411986U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105482862A (en) * | 2015-12-29 | 2016-04-13 | 重庆华川油建装备制造(集团)有限公司 | High pressure high sulfate-resistant skid-mounted separating device |
| CN107961630A (en) * | 2017-11-24 | 2018-04-27 | 上海巴安水务股份有限公司 | A kind of combustion gas filter separator system |
| CN110016373A (en) * | 2019-04-25 | 2019-07-16 | 西安长庆科技工程有限责任公司 | A kind of gas separator with defoaming device |
| CN112239219A (en) * | 2020-07-30 | 2021-01-19 | 内蒙古京泰发电有限责任公司 | Urea hydrolysis ammonia production equipment |
-
2014
- 2014-12-11 CN CN201420783068.7U patent/CN204411986U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105482862A (en) * | 2015-12-29 | 2016-04-13 | 重庆华川油建装备制造(集团)有限公司 | High pressure high sulfate-resistant skid-mounted separating device |
| CN105482862B (en) * | 2015-12-29 | 2018-03-23 | 重庆华川油建装备制造(集团)有限公司 | The high sulfur resistive sledge dress separator of high pressure |
| CN107961630A (en) * | 2017-11-24 | 2018-04-27 | 上海巴安水务股份有限公司 | A kind of combustion gas filter separator system |
| CN110016373A (en) * | 2019-04-25 | 2019-07-16 | 西安长庆科技工程有限责任公司 | A kind of gas separator with defoaming device |
| CN110016373B (en) * | 2019-04-25 | 2024-01-23 | 西安长庆科技工程有限责任公司 | Gas separator with defoaming device |
| CN112239219A (en) * | 2020-07-30 | 2021-01-19 | 内蒙古京泰发电有限责任公司 | Urea hydrolysis ammonia production equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204411986U (en) | Combined separator | |
| JP6246950B2 (en) | Purifier for compressed air | |
| CN102698554A (en) | High-efficiency gas-liquid separator in compressor device | |
| KR101140251B1 (en) | Immersion Scrubber | |
| CN102974187A (en) | Compound anti-channeling gas-liquid separator | |
| RU2469771C1 (en) | Separator for gas purification | |
| RU80768U1 (en) | CENTRIFUGAL GAS-LIQUID SEPARATOR | |
| CN201940134U (en) | Fresh air filter | |
| CN202113731U (en) | High-efficient oil-water separator | |
| CN203639438U (en) | Device for purifying natural gas | |
| US2087219A (en) | Method amd apparatus fok cleaning | |
| CN202876606U (en) | Gas-liquid separator combined with centrifugal separation, baffle plate and filter | |
| CN201959697U (en) | Efficient air filter | |
| CN201959660U (en) | High-efficient ammonia oil removal filter | |
| CN206444360U (en) | A kind of oil removal filter | |
| CN202860347U (en) | Agglomerate cyclone separator | |
| CN103691232B (en) | A kind of gas in natural gas separator with inverted round stage filter core | |
| CN105327575A (en) | Apparatus used for gas-solid separation | |
| CN202645945U (en) | Cyclone agglutination combined separator used before natural gas compressor | |
| RU101936U1 (en) | VERTICAL OIL AND GAS SEPARATOR | |
| CN202892985U (en) | Combined anti-deviating gas-liquid separator | |
| RU116487U1 (en) | INSTALLATION FOR SEPARATION OF AIR AND VAPORS FROM LIQUID | |
| CN202044875U (en) | High-efficiency separator for tail gas of device with sodium nitrate and sodium nitrite | |
| CN202921104U (en) | Gas-liquid separator | |
| RU2469770C1 (en) | Separator for gas purification |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150624 Termination date: 20191211 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |