CN203899209U - Triphase separator - Google Patents
Triphase separator Download PDFInfo
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- CN203899209U CN203899209U CN201420209505.4U CN201420209505U CN203899209U CN 203899209 U CN203899209 U CN 203899209U CN 201420209505 U CN201420209505 U CN 201420209505U CN 203899209 U CN203899209 U CN 203899209U
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- liquid
- separator
- gas
- tank body
- separation
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Abstract
The utility model discloses a triphase separator. The triphase separator comprises a tank body and a material inlet formed in the tank body, wherein a rectifier, a gas separator, an efficient liquid-phase separator, a mechanical liquid-level controller and a demister are sequentially arranged in the tank body from left to right; the demister is connected with a gas outlet; the mechanical liquid-level controller comprises a first liquid inlet and a second liquid inlet which are connected with a first liquid outlet and a second liquid outlet; the internal structure of the tank body is a three-segment structure that the front segment is used for separation and rectification, the middle segment is used for efficient separation and the tail segment adopts a structure with an automatic separation and distribution function. The triphase separator has the characteristics of high efficiency, low energy consumption, accurate control and low labor cost.
Description
Technical field
The utility model belongs to oil-gas-water separator technical field, relates in particular to a kind of three phase separator.
Background technology
Three phase separator of the prior art utilizes gravitational settling and instrument, by-pass valve control to combine, and control mode realization is separated by liquid liquid, the object of gas-liquid separation, control logic is comparatively loaded down with trivial details, precision is low, fluctuation is large, construction and maintenance cost higher, can not meet the requirement of user to the low cost of production equipment, low energy consumption, low manpower supervision demand.
Summary of the invention
The purpose of this utility model is to provide the three phase separator of a kind of low cost, low energy consumption, low manpower supervision demand, to meet user's demand.
In order to realize the purpose of this utility model, the utility model provides a kind of three phase separator, comprise: tank body and be arranged at the material inlet on described tank body, in described tank body, be disposed with from left to right rectifier, gas separator, high efficiency liquid phase separator, mechanical liquid level controller, demister, described demister is connected with gas vent, described mechanical liquid level controller comprises first liquid entrance, second liquid entrance, it is connected with first liquid outlet and second liquid outlet, and it utilizes the poor different liquids that carries out of fluid density automatically to distribute; Wherein said rectifier is used for adjusting fluid flow pattern, and described gas separator is used for carrying out gas phase separation, and described high efficiency liquid phase separator is used for carrying out liquid phase separation, and it promotes granule coalescent according to different liquids to its adsorption agglutinating power difference; Described low density liquid and high density liquid enter described mechanical liquid level controller from described first liquid entrance and described second liquid entrance respectively, and from described first liquid outlet and second liquid outlet, flow out respectively, gas phase enters described demister after described gas separator separation carries out final great Ye and drips separation, and discharges from described gas vent.
The utility model, compared with prior art, because tank interior structure is three stage structure, leading portion: separated, rectification, stage casing: efficiently separated, rear: there is the structure of automatic separated distribution function, therefore, the utlity model has the feature that efficiency is high, energy consumption is low, control is accurate, human cost is low.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
In figure, 1-material inlet, 2-rectifier, 3-gas separator, 4-high efficiency liquid phase separator, 5-demister, 6-gas vent, 7-mechanical liquid level controller, 8-first liquid entrance, 9-second liquid entrance, the outlet of 10-first liquid, the outlet of 11-second liquid.
The specific embodiment
In order to make the purpose of this utility model, technical scheme and beneficial effect clearer, below in conjunction with embodiment, the utility model is further elaborated.Should be understood to specific embodiment described herein only in order to explain the utility model, be not limited to protection domain of the present utility model.
As shown in Figure 1, a kind of three phase separator that the utility model provides, comprise: tank body and be arranged at the material inlet on described tank body, in described tank body, be disposed with from left to right rectifier, gas separator, high efficiency liquid phase separator, mechanical liquid level controller, demister, described demister is connected with gas vent, described mechanical liquid level controller comprises first liquid entrance, second liquid entrance, and it is connected with first liquid outlet and second liquid outlet; Wherein said rectifier is used for adjusting fluid flow pattern, described gas separator is used for carrying out gas phase separation, described high efficiency liquid phase separator is used for carrying out liquid phase separation, described low density liquid and high density liquid enter described mechanical liquid level controller from described first liquid entrance and described second liquid entrance respectively, and from described first liquid outlet and second liquid outlet, flow out respectively, gas phase enters described demister after described gas separator separation carries out final great Ye and drips separation, and discharges from described gas vent.
Above-mentioned high efficiency liquid phase separator is to rely on the poor principle of fluid density to carry out liquid automatically to distribute, and is one of core component in this cover system; The main different liquids that relies on promotes granule coalescent to equipment surface absorption agglutinating power difference, improves the rate of departure, is one of core component in this cover system.
The utility model is applied in crude oil, water, the separating treatment of associated gas or the gas dehydration treatment process in gas field in oil field environment such as natural gas, MEG (ethylene glycol) (or other medium), water separation, and the gas-liquid in process stream, liquid liquid is separated.The utility model utilizes the gravitational settling difference poor with fluid density to carry out related process and calculates to reach the separated object of liquid liquid, and by equipment gas phase channel, increase the equipment such as demister (or miscellaneous equipment) remove natural gas in unnecessary liquid reach the requirement of carrying qualified gas.
When using, material enters three phase separator by material inlet, after liquids and gases carry out initial gross separation after impact enters cowling panel left side, by cowling panel, enters right side separated space (cowling panel effect is to adjust fluid flow pattern); After gas phase separation, entering demister carries out final great Ye and drips the separation middle liquid content of guaranteeing to give vent to anger, liquid phase is carried out parting liquid by high efficiency liquid phase separator and is separated and enters mechanical liquid level controller, low-density medium from upside enter, high-density medium enters respectively and stores bin and then from outlet, flow out from downside enters mechanical liquid level controller.
The above is only preferred embodiment of the present utility model; it should be pointed out that for those skilled in the art, do not departing under the prerequisite of the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (1)
1. a three phase separator, it is characterized in that, comprise: tank body and be arranged at the material inlet on described tank body, in described tank body, be disposed with from left to right rectifier, gas separator, high efficiency liquid phase separator, mechanical liquid level controller, demister, described demister is connected with gas vent, described mechanical liquid level controller comprises first liquid entrance, second liquid entrance, it is connected with first liquid outlet and second liquid outlet, and it utilizes the poor different liquids that carries out of fluid density automatically to distribute; Wherein said rectifier is used for adjusting fluid flow pattern, and described gas separator is used for carrying out gas phase separation, and described high efficiency liquid phase separator is used for carrying out liquid phase separation, and it promotes granule coalescent according to different liquids to its adsorption agglutinating power difference; Described low density liquid and high density liquid enter described mechanical liquid level controller from described first liquid entrance and described second liquid entrance respectively, and from described first liquid outlet and second liquid outlet, flow out respectively, gas phase enters described demister after described gas separator separation carries out final great Ye and drips separation, and discharges from described gas vent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420209505.4U CN203899209U (en) | 2014-04-28 | 2014-04-28 | Triphase separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420209505.4U CN203899209U (en) | 2014-04-28 | 2014-04-28 | Triphase separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203899209U true CN203899209U (en) | 2014-10-29 |
Family
ID=51773502
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420209505.4U Expired - Fee Related CN203899209U (en) | 2014-04-28 | 2014-04-28 | Triphase separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203899209U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111617515A (en) * | 2020-05-15 | 2020-09-04 | 浙江大学 | Gas-liquid-solid three-phase separation device and separation method based on array sensor |
| CN113893619A (en) * | 2021-10-27 | 2022-01-07 | 中国石油化工股份有限公司 | Gas-liquid separator |
-
2014
- 2014-04-28 CN CN201420209505.4U patent/CN203899209U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111617515A (en) * | 2020-05-15 | 2020-09-04 | 浙江大学 | Gas-liquid-solid three-phase separation device and separation method based on array sensor |
| CN113893619A (en) * | 2021-10-27 | 2022-01-07 | 中国石油化工股份有限公司 | Gas-liquid separator |
| CN113893619B (en) * | 2021-10-27 | 2023-01-03 | 中国石油化工股份有限公司 | Gas-liquid separator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 300457 Tianjin Binhai New Area of Tianjin economic and Technological Development Zone t-win Village 8, building 709, room 710, Raycom Patentee after: Tianjin grandwell made Technology Co. Ltd. Address before: 300457 Tianjin Binhai New Area of Tianjin economic and Technological Development Zone t-win Village 8, building 709, room 710, Raycom Patentee before: TIANJIN LIANHUI OIL AND GAS TECHNOLOGY CO., LTD. |
|
| 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: 20141029 Termination date: 20180428 |