CN203777870U - Gas-liquid separator - Google Patents
Gas-liquid separator Download PDFInfo
- Publication number
- CN203777870U CN203777870U CN201420104731.6U CN201420104731U CN203777870U CN 203777870 U CN203777870 U CN 203777870U CN 201420104731 U CN201420104731 U CN 201420104731U CN 203777870 U CN203777870 U CN 203777870U
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- tank body
- gas
- liquid
- flow distribution
- distribution plate
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- Separating Particles In Gases By Inertia (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model relates to a gas-liquid separator which comprises an upper tank body and a lower tank body, wherein the upper tank body and the lower tank body are connected in a sealing manner to form an integrated tank body; a liquid collecting area, a liquid condensing area, a shunting area, a rising area and a gas collecting area are arranged on the tank body from bottom to top; the liquid collecting area is communicated with liquid discharging openings in the bottom and the side; a lower wire mesh demister is arranged at the liquid condensing area; an upper shunting plate and a lower shunting plate are arranged at the shunting area which is communicated with a mixed gas-liquid inlet; an upper wire mesh demister and a filtration core are arranged at the rising area. The gas-liquid separator has the advantages of being reasonable in structure, high in separation efficiency, complete in separation, sufficient in gas purification, easy and convenient to assemble and maintain and wide in application, and realizes separation and filtration.
Description
Technical field
The utility model relates to gas-liquid separation technology, is particularly widely used in a kind of gas-liquid separator of the industries such as chemical industry, food, pharmacy, oil, water treatment, metallurgy.
Background technology
Gas-liquid separator is to utilize gas-liquid proportion difference, and under same volume, the quality of gas is less than the quality of liquid.In the container of a sudden enlargement, after flow velocity reduces, in the process turning in main fluid, in gas phase, trickle drop sinks and separated from the gas, realizes lime set and reclaims or gas phase purifying.
The normal separation method adopting of tradition gas-liquid separator has: gravitational settling, baffling separation, centrifugal force separate, silk screen separation, ultra-filtration and separation etc.According to the difference of performance and structure, be applicable to respectively different industries.Adopt the gas-liquid separator of single partition method all to have shortcoming separately, gravity separator separative efficiency is low, and equipment volume is huge, takes up room many.Deflection separator, separator using centrifugal force, silk screen separator and ultra-filtration and separation device equipment volume are little, and separative efficiency is higher, but segregational load narrow range exceedes after gas-liquid mixture regulation flow velocity, and separative efficiency sharply declines.In the time that segregational load is greater than load range, easily produces and separate not thoroughly gas with liquid phenomenon.
Summary of the invention
In order to overcome the shortcoming of existing gas-liquid separator, the utility model provides a kind of and adopts multiple separation method in the Novel gas-liquid separator of one.Have rational in infrastructurely, separative efficiency is high, separate thoroughly, and fully Purge gas, installation and maintenance are easy, advantage applied widely, to realize separating and filtering.
For achieving the above object, the utility model is achieved through the following technical solutions:
A kind of gas-liquid separator, comprises upper tank body, lower tank two parts, and it is a complete tank body that upper tank body and lower tank are tightly connected; Tank body is provided with liquid collecting zone, lime set district, shunting zone, rising area, gas collection district from bottom to top; Liquid collecting zone communicates with bottom leakage fluid dram and side leakage fluid dram; Lime set district is provided with lower wire mesh demister, and shunting zone is provided with flow distribution plate and lower flow distribution plate, and gas-liquid mixture import communicates with shunting zone, and rising area is provided with wire mesh demister and filter core, and gas collection district communicates with exhaust outlet; Gas-liquid mixture import is arranged on tank body middle part, position between upper flow distribution plate and lower flow distribution plate; Bottom leakage fluid dram is arranged on tank base, and side leakage fluid dram is arranged on tank body side lower part; Exhaust outlet is arranged on tank body top.
Upper tank body top is provided with safety valve and Pressure gauge; Upper tank body bottom is provided with base plate, and filter core is fixed with removably and base plate, and base plate middle part is provided with the through hole that can discharge for rising area gas; After upper tank body and lower tank are tightly connected, filter core is arranged in tank chamber; Between upper tank body base plate and upper tank body, form gas collection district.
Described upper wire mesh demister and lower wire mesh demister, it is that the gauze pad of 100mm～200mm forms that the wire that is 0.05mm～0.25mm by diameter (various stainless steel wires, galvanized wire, copper wire, nickel wire, titanium silk, B alloy wire etc.) or nonmetal wire (Polyamide Yarns, polyethylene filament, polyacrylic fibres etc.) weave and build up thickness.
Described upper flow distribution plate and lower flow distribution plate are circular table dividing plate.Dividing plate is provided with some apertures, and the dividing plate conical surface is provided with the blade that is parallel to the conical surface.Lower flow distribution plate is horizontally placed in tank chamber, and upper flow distribution plate is horizontally placed in tank chamber with inverted-cone.
Compared with prior art, the beneficial effect having is the utility model:
1) a kind of gas-liquid mixture of gas-liquid separator enters into after tank body, the baffling centrifugation of flow distribution plate and lower flow distribution plate on passing through in shunting zone, and mist carries out gas-liquid separation for the first time, and isolated gas rises and enters rising area, and liquid condensation enters liquid collecting zone.
The mist slowing down through shunting zone flow velocity carries out gas-liquid separation for the second time through the effect of gravitational settling again.Mist continues to sink and utilizes the principle of silk screen separation to carry out gas-liquid separation for the third time through lower wire mesh demister.The liquid of cohesion enters into liquid collecting zone.
While entering into the upper wire mesh demister of mist process of rising area, the principle of utilizing silk screen to separate is carried out the 4th gas-liquid separation.Isolated all gas utilizes ultra-filtration and separation principle to carry out the 5th gas-liquid separation by filter core.
2) liquid collecting zone is provided with end leakage fluid dram and side leakage fluid dram, can adopt the discharge opeing of side exhaust outlet in the time that separation has impurity gaseous mixture, and end leakage fluid dram is discharged impurity.Expand the scope of application.
3) upper tank body top is provided with safety valve and Pressure gauge, can intuitively observe tank body internal pressure, safety valve releasing pressure automatically in the time exceeding tank body pressure.Ensure separator trouble free service.Can be used as (height) pressure vessel.Expand the scope of application.
4) adopt multi-stage separation, utilize multiple separation principle, realize separative efficiency high, separate thoroughly.Gas liquid content after separation is extremely low, has solved gas with liquid phenomenon, reaches the effect of Purge gas.Owing to adopting multi-stage separation, ensure to enter into the when flow velocity of gas-liquid of filter core, reduce filter core resistance, extend the service life of filter core.There is the effect of separating and filtering.Tank body of the present utility model adopts separate type, facilitates installation, maintenance, maintenance.
Brief description of the drawings
Fig. 1 is the structural representation of a kind of gas-liquid separator of the utility model.
Fig. 2 is the lower flow distribution plate schematic diagram of a kind of gas-liquid separator of the utility model.
In figure: the upper wire mesh demister 15-filter core 16-exhaust outlet 17-safety valve 18-Pressure gauge 19-base plate of the upper flow distribution plate 14-of flow distribution plate 13-under wire mesh demister 12-under the leakage fluid dram 10-side leakage fluid dram 11-of 6-rising area, 5-shunting zone, 4-lime set district, 1-upper tank body 2-lower tank 3-liquid collecting zone 7-gas collection district 8-gas-liquid mixture import 9-bottom
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is further illustrated:
A kind of gas-liquid separator, comprises upper tank body 1, lower tank 2 two parts.It is a complete tank body that upper tank body 1 and lower tank 2 are tightly connected.Tank body is provided with liquid collecting zone 3, lime set district 4, shunting zone 5, rising area 6, gas collection district 7 from bottom to top.Liquid collecting zone 3 communicates with bottom leakage fluid dram 9 and side leakage fluid dram 10.Lime set district 4 is provided with lower wire mesh demister 11.Shunting zone 5 is provided with flow distribution plate 13 and lower flow distribution plate 12, and gas-liquid mixture import 8 communicates with shunting zone 5.Rising area 6 is provided with wire mesh demister 14 and filter core 15.Gas collection district 7 communicates with exhaust outlet 16.
Described gas-liquid mixture import 8 is arranged on tank body middle part, position between upper flow distribution plate 13 and lower flow distribution plate 12.Bottom leakage fluid dram 9 is arranged on tank base, and side leakage fluid dram 10 is arranged on tank body side lower part.Exhaust outlet 16 is arranged on tank body top.
Described upper tank body top is provided with safety valve 17 and Pressure gauge 18.Upper tank body bottom is provided with base plate 19, and filter core 15 is fixing with removably and base plate 19, and base plate 19 middle parts are provided with the through hole that can discharge for rising area gas.After upper tank body 1 is closely connected with lower tank 2, filter core 15 is arranged in tank chamber.Upper tank body base plate 19 and upper tank body 1 between form gas collection district.
Described upper wire mesh demister 14 and lower wire mesh demister 11, the gauze pad that is woven and built up 100mm～200mm by the wire (various stainless steel wires, galvanized wire, copper wire, nickel wire, titanium silk, B alloy wire etc.) of 0.05mm～0.25mm or nonmetal wire (Polyamide Yarns, polyethylene filament, polyacrylic fibres etc.) forms.
Described upper flow distribution plate 13 and lower flow distribution plate 12 are circular table dividing plate.Dividing plate is provided with some apertures, and the dividing plate conical surface is provided with the blade that is parallel to the conical surface.Lower flow distribution plate 12 is horizontally placed in tank chamber, and upper flow distribution plate 13 is horizontally placed in tank chamber with inverted-cone.
The course of work of the present utility model is as follows:
Gas-liquid mixture enters shunting zone after entering into tank body by gas-liquid mixture import 8, in process when flow distribution plate 13 and lower flow distribution plate 12, gas baffling and walking, liquid is separated from the gas by effect of inertia, liquid collects downwards along flow distribution plate wooden partition under Action of Gravity Field, mist is realized gas-liquid separation for the first time, and isolated gas rises and enters rising area, and liquid condensation enters liquid collecting zone.
The mist slowing down through shunting zone flow velocity carries out gas-liquid separation for the second time through the effect of gravitational settling again.Mist continues to sink through lower wire mesh demister 11, and liquid is stopped downwards and collects by silk screen, realizes gas-liquid separation for the third time.The liquid of cohesion enters into liquid collecting zone.Finally discharge tank body by bottom leakage fluid dram 9 and side leakage fluid dram 10.
Enter into rising area through the gas of first, second and third separation, in process, when wire mesh demister 14, liquid is stopped to collect downwards by silk screen realizes the 4th gas-liquid separation.Isolated all gas more after filtration filter core 15 realize the 5th gas-liquid separation.Final isolated gas is discharged tank body through exhaust outlet 16.
Liquid collecting zone is provided with bottom leakage fluid dram 9 and side leakage fluid dram 10, can adopt 10 discharge opeings of side leakage fluid dram in the time that separation has impurity gaseous mixture, and bottom leakage fluid dram 9 is discharged impurity.
Above, be only general principle of the present utility model, not the utility model imposed any restrictions, everyly according to the utility model, it is carried out to equivalent variations and modification, all within the category of the art of this patent protection scheme.
Claims (4)
1. a gas-liquid separator, is characterized in that, comprises upper tank body, lower tank two parts, and it is a complete tank body that upper tank body and lower tank are tightly connected; Tank body is provided with liquid collecting zone, lime set district, shunting zone, rising area, gas collection district from bottom to top; Liquid collecting zone communicates with bottom leakage fluid dram and side leakage fluid dram; Lime set district is provided with lower wire mesh demister, and shunting zone is provided with flow distribution plate and lower flow distribution plate, and gas-liquid mixture import communicates with shunting zone, and rising area is provided with wire mesh demister and filter core, and gas collection district communicates with exhaust outlet; Gas-liquid mixture import is arranged on tank body middle part, position between upper flow distribution plate and lower flow distribution plate; Bottom leakage fluid dram is arranged on tank base, and side leakage fluid dram is arranged on tank body side lower part; Exhaust outlet is arranged on tank body top.
2. a kind of gas-liquid separator according to claim 1, is characterized in that, upper tank body top is provided with safety valve and Pressure gauge; Upper tank body bottom is provided with base plate, and filter core is fixed with removably and base plate, and base plate middle part is provided with the through hole that can discharge for rising area gas; After upper tank body and lower tank are tightly connected, filter core is arranged in tank chamber; Between upper tank body base plate and upper tank body, form gas collection district.
3. a kind of gas-liquid separator according to claim 1, is characterized in that, upper wire mesh demister and lower wire mesh demister, and it is that the gauze pad of 100mm～200mm forms that the wire that is 0.05mm～0.25mm by diameter or nonmetal wire weave and build up thickness.
4. a kind of gas-liquid separator according to claim 1, is characterized in that, upper flow distribution plate and lower flow distribution plate are circular table dividing plate; Dividing plate is provided with some apertures, and the dividing plate conical surface is provided with the blade that is parallel to the conical surface; Lower flow distribution plate is horizontally placed in tank chamber, and upper flow distribution plate is horizontally placed in tank chamber with inverted-cone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420104731.6U CN203777870U (en) | 2014-03-07 | 2014-03-07 | Gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420104731.6U CN203777870U (en) | 2014-03-07 | 2014-03-07 | Gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203777870U true CN203777870U (en) | 2014-08-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420104731.6U Expired - Fee Related CN203777870U (en) | 2014-03-07 | 2014-03-07 | Gas-liquid separator |
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| Country | Link |
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| CN (1) | CN203777870U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104548840A (en) * | 2014-12-18 | 2015-04-29 | 广西大学 | Gas-liquid separator for preparing high-purity shale gas through compression and liquefaction |
| CN106186137A (en) * | 2016-09-30 | 2016-12-07 | 北京凌锐能源技术有限公司 | A kind of aqueous vapor trash eliminator |
| CN106583356A (en) * | 2016-11-22 | 2017-04-26 | 启东兴东石化设备制造有限责任公司 | Gas blocking pressure stabilizer |
| CN107019963A (en) * | 2017-05-19 | 2017-08-08 | 苏州奥尔新能源科技有限公司 | A kind of New Hydrogen/oxygen separating device |
| CN108072212A (en) * | 2017-11-04 | 2018-05-25 | 上海佑伏吸附制冷有限公司 | Gas-liquid separation and pressure equaliser occur for a kind of ammonium hydroxide for spraying generator |
-
2014
- 2014-03-07 CN CN201420104731.6U patent/CN203777870U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104548840A (en) * | 2014-12-18 | 2015-04-29 | 广西大学 | Gas-liquid separator for preparing high-purity shale gas through compression and liquefaction |
| CN106186137A (en) * | 2016-09-30 | 2016-12-07 | 北京凌锐能源技术有限公司 | A kind of aqueous vapor trash eliminator |
| CN106583356A (en) * | 2016-11-22 | 2017-04-26 | 启东兴东石化设备制造有限责任公司 | Gas blocking pressure stabilizer |
| CN106583356B (en) * | 2016-11-22 | 2019-03-01 | 启东兴东石化设备制造有限责任公司 | Choke voltage-stablizer |
| CN107019963A (en) * | 2017-05-19 | 2017-08-08 | 苏州奥尔新能源科技有限公司 | A kind of New Hydrogen/oxygen separating device |
| CN108072212A (en) * | 2017-11-04 | 2018-05-25 | 上海佑伏吸附制冷有限公司 | Gas-liquid separation and pressure equaliser occur for a kind of ammonium hydroxide for spraying generator |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140820 |