CN201329199Y - Multi-level gas-liquid separating device - Google Patents
Multi-level gas-liquid separating device Download PDFInfo
- Publication number
- CN201329199Y CN201329199Y CNU200820303619XU CN200820303619U CN201329199Y CN 201329199 Y CN201329199 Y CN 201329199Y CN U200820303619X U CNU200820303619X U CN U200820303619XU CN 200820303619 U CN200820303619 U CN 200820303619U CN 201329199 Y CN201329199 Y CN 201329199Y
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- cylindrical shell
- liquid
- cylinder
- gas
- barretter
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Abstract
The utility model discloses a multi-level gas-liquid separating device, which comprises a cylinder (1), wherein the top part of the cylinder (1) is provided with an exhausting opening (2), and a liquid collecting plate (3) is arranged below the exhausting opening (2); the side wall of the cylinder (1) is provided with a flow stabilizing pipe (4), and one end which is arranged outside the cylinder of the flow stabilizing pipe (4) is connected with a conical diffusion pipe (5); and the end which is arranged inside the cylinder of the flow stabilizing pipe (4) is closed, and the wall which is arranged inside the cylinder of the flow stabilizing pipe (4) is connected with an exhaust stack (6) which is formed by serially joining two or more levels, and a jet current control tube (7) is arranged outside the exhaust stack (6). Through the multi-level inflation and the multi-level separation, two phases inside the medium are adequately separated from each other, so that the liquid height can be effectively controlled, thereby realizing the separation effect. The multi-level gas-liquid separating device has the advantages of simple structure and convenient operation.
Description
Technical field
The utility model relates to a kind of multi-stage gas-liquid separator, belongs to the gas-liquid separation technical field.
Background technology
The gas-liquid separation technology is indispensable in many technical process, gas-liquid separating method commonly used at present is absorption type, filtering type and combined type etc., according to medium and process conditions design separator, the separator type has silk screen, filler, whirlwind, baffle plate etc. usually; Silk screen and filler separator are had relatively high expectations to separating medium, and the separating treatment amount is lower; The whirlwind treating capacity is big, but separating effect is undesirable, and restricted to dielectric viscosity; Baffle arrangement is simple, but separating effect is bad.Said apparatus is that complex structure is unfavorable for promoting a bit, and also some is the price height, has increased equipment investment cost.Therefore, existing gas-liquid separation technology still is not ideal enough.
The utility model content
The purpose of this utility model is, a kind of simple in structure, multi-stage gas-liquid separator that cost is low, easy to operate is provided, it fully separates two phase constituents in the medium by multiple expansion and multi-stage separation, and can effectively control liquid level, reaches separating effect.
The utility model is to constitute like this: it comprises cylindrical shell, and the top of cylindrical shell is provided with exhaust outlet, and the exhaust outlet below is provided with liquid collecting plate; The sidewall of cylindrical shell is provided with barretter, and the end of barretter outside tube is connected with conic diffuse; The end sealing of barretter in tube, the tube wall of barretter in tube is connected with the exhaust stack of contacting more than the two-stage, and exhaust stack is provided with the jet control valve outward.
In the above-mentioned multi-stage gas-liquid separator, bottom one side of described cylindrical shell is provided with the discharge opeing bend pipe, the nearly cylindrical shell of the termination of discharge opeing bend pipe in cylindrical shell bottom, and the end of discharge opeing bend pipe outside cylindrical shell is connected with the liquid surface height controlling pipe.
In the aforesaid multi-stage gas-liquid separator, described cylindrical shell bottom is provided with discharge orifice.
Compared with prior art, the utility model fully separates two phase constituents in the medium by multiple expansion and multi-stage separation, and can effectively control liquid level, reaches separating effect.The utility model goes for multiple vapour-liquid medium, and the medium bigger to viscosity also can reach the vapor-liquid separation effect, and the adjusting that the utility model can carry out inlet flow rate according to different operating modes just can continuous operation; In addition, the utility model also has simple in structure, easy to operate, economical and practical advantage.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Being labeled as in the accompanying drawing: the 1-cylindrical shell, the 2-exhaust outlet, the 3-liquid collecting plate, the 4-barretter, 5 conic diffuses-, 6-exhaust stack, 7-jet control valve, 8-discharge opeing bend pipe, 9-liquid surface height controlling pipe, 10-discharge orifice.
The specific embodiment
The utility model is described in further detail below in conjunction with drawings and Examples, but not as the foundation of the utility model being done any restriction.
Embodiment of the present utility model: as shown in Figure 1, it comprises cylindrical shell 1, is provided with exhaust outlet 2 at the top of cylindrical shell 1, is provided with liquid collecting plate 3 below exhaust outlet 2; Sidewall at cylindrical shell 1 is provided with barretter 4, and the end of barretter 4 outside tube is connected with conic diffuse 5; With the end sealing of barretter 4 in tube, the tube wall of barretter 4 in tube is connected with the exhaust stack 6 of contacting more than the two-stage, outside exhaust stack 6, be provided with jet control valve 7; A side is provided with discharge opeing bend pipe 8 in the bottom of cylindrical shell 1, and makes the nearly cylindrical shell of the termination of discharge opeing bend pipe 8 in cylindrical shell 11 bottom, the end of discharge opeing bend pipe 8 outside cylindrical shell 1 is connected with liquid surface height controlling pipe 9, produces discharge orifice 10 then in cylindrical shell 1 bottom.
Gas-liquid separating method of the present utility model is by conic diffuse the gas in the medium to be expanded rapidly earlier, through through multistage exhaust stack the medium multi-stage diffluence being injected on the jet control valve inwall again behind the current stabilization, forms tubular gas-liquid post; Liquid is collected by cylindrical shell; Medium after initial gross separation is arranged on the liquid collecting plate absorption at cylindrical shell top once more in uphill process, separate once more; Gas after the separation is discharged from outlet.After described liquid was collected by cylindrical shell, because the liquid of collecting has different temperatures in different aspects, the process that rises at hot-fluid formed thermal cycle, makes that the gas in the liquid of having collected is further separated out, and residual gas is separated.Cylindrical shell is provided with the fluid control valve with the liquid level in effective control cylindrical shell, and liquid is flowed out automatically.
Operation principle of the present utility model is as follows:
The medium that need separate enters by the inlet of conic diffuse 5, in conic diffuse, make the gaseous state volumetric expansion of medium, in barretter, reach current stabilization and enter multistage exhaust stack, medium is injected on the jet control valve inwall through multi-stage diffluence, and formation tubular gas-liquid post enters cylindrical shell and carries out diffusing the second time expansion; Because medium through in advance expansion, current stabilization, multistage radiation, makes the active gas liquid high-efficiency that reaches of gas phase media separate; Gas rises and meets liquid collecting plate absorption drop, forms gas-liquid and separates once more, and the gas after the separation is discharged from exhaust outlet; The liquid that enters cylindrical shell bottom particularly thermal medium forms different medium aspects, and hot-fluid rises and forms thermal cycle and also the gas of upper surface is separated out, and residual gas is separated; The level control pipe can effectively be controlled liquid level, makes medium keep certain height in cylindrical shell, reaches from current control.Main feature of the present utility model: by multiple expansion and multi-stage separation two phase constituents in the medium are fully separated, and can effectively control liquid level, reach separating effect.
Claims (3)
1. multi-stage gas-liquid separator, it is characterized in that: comprise cylindrical shell (1), the top of cylindrical shell (1) is provided with exhaust outlet (2), and exhaust outlet (2) below is provided with liquid collecting plate (3); The sidewall of cylindrical shell (1) is provided with barretter (4), and the end of barretter (4) outside tube is connected with conic diffuse (5); The end sealing of barretter (4) in tube, the tube wall of barretter (4) in tube is connected with the exhaust stack of contacting more than the two-stage (6), the outer jet control valve (7) that is provided with of exhaust stack (6).
2. multi-stage gas-liquid separator according to claim 1, it is characterized in that: bottom one side of described cylindrical shell (1) is provided with discharge opeing bend pipe (8), a termination nearly cylindrical shell (1) bottom of discharge opeing bend pipe (8) in cylindrical shell (1), the end of discharge opeing bend pipe (8) outside cylindrical shell (1) is connected with liquid surface height controlling pipe (9).
3. multi-stage gas-liquid separator according to claim 1 is characterized in that: described cylindrical shell (1) bottom is provided with discharge orifice (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200820303619XU CN201329199Y (en) | 2008-12-23 | 2008-12-23 | Multi-level gas-liquid separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU200820303619XU CN201329199Y (en) | 2008-12-23 | 2008-12-23 | Multi-level gas-liquid separating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201329199Y true CN201329199Y (en) | 2009-10-21 |
Family
ID=41222572
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU200820303619XU Expired - Lifetime CN201329199Y (en) | 2008-12-23 | 2008-12-23 | Multi-level gas-liquid separating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201329199Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101757838B (en) * | 2008-12-23 | 2012-12-05 | 贵阳铝镁设计研究院有限公司 | Method and device for multi-stage gas-liquid separation |
-
2008
- 2008-12-23 CN CNU200820303619XU patent/CN201329199Y/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101757838B (en) * | 2008-12-23 | 2012-12-05 | 贵阳铝镁设计研究院有限公司 | Method and device for multi-stage gas-liquid separation |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: GUIYANG ALUMINUM AND MAGNESIUM DESIGN INSTITUTE CO Free format text: FORMER OWNER: GUIYANG ALUMINIUM AND MAGNESIUM DESIGN INST. Effective date: 20110721 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 550004 NO. 208, BEIJING ROAD, GUIYANG CITY, GUIZHOU PROVINCE TO: 550081 NO.2, JINZHU ROAD, JINYANG NEW DISTRICT, GUIYANG CITY, GUIZHOU PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20110721 Address after: 550081 Guiyang Province, Jinyang New District, Zhu Zhu Road, No. 2 Patentee after: Guiyang Aluminum & Magnesium Design Institute Co., Ltd. Address before: 550004 No. 208, Beijing Road, Guiyang, Guizhou Patentee before: Guiyang Aluminium and Magnesium Design Inst. |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20091021 Effective date of abandoning: 20081223 |
|
| RGAV | Abandon patent right to avoid regrant |