CN201959692U - Gas-liquid separation system - Google Patents
Gas-liquid separation system Download PDFInfo
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- CN201959692U CN201959692U CN2010206158073U CN201020615807U CN201959692U CN 201959692 U CN201959692 U CN 201959692U CN 2010206158073 U CN2010206158073 U CN 2010206158073U CN 201020615807 U CN201020615807 U CN 201020615807U CN 201959692 U CN201959692 U CN 201959692U
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Abstract
The utility model relates to a gas-liquid separation system, which comprises a raw-liquid inlet pipe (I), a pre-separator (A), a spiral-flow type gas-liquid separator (B) and a spray catcher (C), wherein the pre-separator (A) comprises a first columnar-cylinder body (1); a first input pipe (11) and a first liquid-outlet pipe (12) are arranged on the first columnar-cylinder body (1); the spiral-flow type gas-liquid separator (B) comprises a second columnar-cylinder body (2); a second gas-outlet pipe (22), a second input pipe (21) and a second liquid-outlet pipe (23) are arranged on the second columnar-cylinder body (2); the top of the raw-liquid inlet pipe (I) is communicated with a first end (21a) of the second input pipe (21); the middle part of the second input pipe (21) is communicated with the first input pipe (11); and the second gas-outlet pipe (22) is communicated with a third input pipe (31) of the spray catcher (C). Compared with the prior art, the gas-liquid separation system has the advantages that the separation effect is very ideal, the purity of separated-phase matter is higher, the gas-liquid separation system has higher metering capability and has pre-separation effect on liquid-phase matter, and the working efficiency is very high in case of less content of gas-phase matter.
Description
Technical field
The utility model belongs to the technical field that fluid separates, and is meant a kind of Separate System of Water-jet that can finally realize gas, liquid two-phase separation especially.
Background technology
In the surface gathering system of oil field, mainly use various separators at present, the natural gas in the oil well produced gas-liquid mixture is separated with oil water mixture, realize the liquid metering then or produce metering.Traditional gas-liquid separator only relies on gravity and realizes the separation of gas, liquid naturally, and air content still is higher in Shu Chu the liquid at last, and separating effect is not ideal enough, and separating rate is slow, and efficient is lower.
For improving the purity of separating the phase thing, guarantee separating property, existing many gas-liquid separators in usefulness, they are by a device or equipment mostly, adopt some physical treatment process,, and realize that two of gas and liquid is separated such as gravitational method, centrifugal process, air supporting method, filtration method and membrane separation process etc.As the patent No. is the Chinese utility model patent " a kind of spiral-flow type gas-liquid separator " of ZL200720108504.0 (publication number is CN201055811Y), and disclosed is a kind of by rotating the gas-liquid separator that gas-liquid mixture relies on centrifugal force separation gas phase thing and liquid phase thing at a high speed.The volume of this spiral-flow type gas-liquid separator is little, separating rate is fast, effective, and have development potentiality preferably.It includes cylindrical barrel body, the top of this cylindrical barrel body sidewall, middle part, bottom are respectively arranged with escape pipe, crude oil input pipe, the drain pipe that is connected with cylindrical barrel body, wherein, the relative cylindrical barrel body of crude oil input pipe is tilted to down, and tangent with the sidewall of cylindrical barrel body.This gas-liquid separator makes gas-liquid mixture can form eddy flow in cylindrical barrel body by the crude oil input pipe under being tilted to, and gas and fluid separation applications are come, and realizes gas-liquid separation.In the practice, gas is in the high speed rotary course, easily drop is taken out of, it is more to contain liquid in the gas phase thing of feasible last output, separating effect still is not ideal enough, and runs into the less gas-liquid mixture of gas content, if still be passed in the spiral-flow type gas-liquid separator uniformly, operating efficiency is not very high, thereby requires further improvement.
The utility model content
Technical problem to be solved in the utility model is to provide a kind of Separate System of Water-jet at the present situation of prior art, its separating effect is very good, it is higher to separate phase thing purity, has higher metering ability, and the liquid phase thing had the pre-separation effect, for the less situation of gas phase thing content, operating efficiency is very high.
The utility model solves the problems of the technologies described above the technical scheme that is adopted: this Separate System of Water-jet is characterized in that: comprise a stoste input pipe, a preseparator, a spiral-flow type gas-liquid separator and a mist eliminator;
Wherein, described preseparator comprises first cylindrical barrel body, and the top of this first cylindrical barrel body is provided with first input pipe, the bottom is provided with first drain pipe, and this first input pipe while is as the outlet of the inlet and the gas of liquid;
Described spiral-flow type gas-liquid separator comprises second cylindrical barrel body, the barrel of this second cylindrical barrel body portion from top to bottom is disposed with second escape pipe, second input pipe, second drain pipe, and relative second cylindrical barrel body of second end of this second input pipe is tilted to down and is tangent with the sidewall of second cylindrical barrel body;
Described stoste input pipe is provided with straight up, and first end of its top and second input pipe is connected, and the middle part of this second input pipe then is connected with first input pipe;
Described mist eliminator comprises tank body, and this tank body top is provided with that the 3rd escape pipe, sidewall are provided with the 3rd input pipe, the bottom is provided with the 3rd drain pipe, and second escape pipe on described second cylindrical barrel body is connected with the 3rd input pipe.
Above-mentioned preseparator, spiral-flow type gas-liquid separator and mist eliminator can adopt existing various technology, wherein, gas-liquid mixture upwards is input to second input pipe from the bottom of stoste input pipe, by the gravity effect, the liquid phase thing is positioned at the below of gas phase thing naturally, by being tilted to down second input pipe that is provided with, the liquid phase thing will enter into preseparator naturally mostly, and preseparator is that the pre-separation of gas-liquid mixture is handled;
The gas-liquid mixture that described spiral-flow type gas-liquid separator will tangentially be imported separates, and gas is exported from second escape pipe, and liquid is exported from second drain pipe, can conflux with first drain pipe of preseparator and unified metering;
Described mist eliminator just will carry out further gas from the gas of second escape pipe output, liquid separates, carry out the final metering of gas phase thing from the gas of the 3rd escape pipe output, conflux and unified metering from the liquid of the 3rd drain pipe output with second drain pipe of spiral-flow type gas-liquid separator.
Collection purity for the gas that guarantees the spiral-flow type gas-liquid separator, reduce last output gas with drop, can carry out following improvement: in described spiral-flow type gas-liquid separator, the port of export of this second escape pipe is opened the side wall upper part at second cylindrical barrel body, the entrance point of the 3rd escape pipe extend into central authorities in the top of second cylindrical barrel body from bottom to top, and, above the 3rd escape pipe entrance point, also be provided with a umbrella top cover, between umbrella top cover and entrance point, be connected with support bar.So, drop runs into the umbrella top cover and just can condense upon on the umbrella top cover, and mentions from the purity of the gas phase thing of second escape pipe output.
Preferably, can be provided with a pair of liquid level gauge on described second cylindrical barrel body, with stable control spiral-flow type gas-liquid separator.
Catch the effect of drop for improving mist eliminator, realize good gas-liquid separation effect, described mist eliminator can be a spiral-flow type mist eliminator, particularly: the sidewall of the 3rd input pipe and tank body is tangent, and described the 3rd escape pipe extend into the central interior of tank body from the top of tank body, the bottom end opening of the 3rd escape pipe and as the inlet of the 3rd escape pipe.This mist eliminator gas-liquid flow is unobstructed logical, makes the processing speed of tank body significantly to increase, thereby can improve the operating efficiency of mist eliminator.
The gas that is entrained with drop tangentially is input in the tank body of mist eliminator, and at tank body generation eddy flow, utilize action of centrifugal force, relatively heavier drop is thrown to inner tank wall and flow into the 3rd drain pipe of tank base along inwall, lighter gas then is pooled to tank body central authorities relatively, the bottom opening of the 3rd escape pipe of central authorities enters into the 3rd escape pipe in extending into tank body, carries out the final metering of gas phase thing from the top output of the 3rd escape pipe at last.
Because the mist eliminator volume is less relatively, the bottom of described mist eliminator tank body can be provided with a support, in order to the high whole mist eliminator of frame.
Compared with prior art, the utility model is by the cooperation of preseparator, spiral-flow type gas-liquid separator, mist eliminator and second input pipe that is obliquely installed, separating effect is very good, it is higher to separate phase thing purity, has higher metering ability, simultaneously, preseparator in the utility model Separate System of Water-jet, gas-liquid mixture pre-separation can be carried out,, the operating efficiency of entire system can be obviously improved for the less situation of gas phase thing content.In addition, mist eliminator seizure drop ability is strong, and work of treatment efficient is very high.
Description of drawings
Fig. 1 is the structural representation of the utility model embodiment;
Fig. 2 is the structural representation of preseparator among the utility model embodiment;
Fig. 3 is the structural representation of spiral-flow type gas-liquid separator among the utility model embodiment;
Fig. 4 is the structural representation of mist eliminator among the utility model embodiment.
The specific embodiment
Embodiment describes in further detail the utility model below in conjunction with accompanying drawing.
As Fig. 1～shown in Figure 4, this Separate System of Water-jet comprises a stoste input pipe I, a preseparator A, a spiral-flow type gas-liquid separator B and a mist eliminator C.
Wherein, as shown in Figure 2, described preseparator A comprises first cylindrical barrel body 1, the top of this first cylindrical barrel body 1 is provided with first input pipe 11, the bottom is provided with first drain pipe 12, the below of this first cylindrical barrel body 1 was provided with bearing 13 and supported whole preseparator A as the outlet of the inlet and the gas of liquid these 11 whiles of first input pipe.
As shown in Figure 3, described spiral-flow type gas-liquid separator B comprises second cylindrical barrel body 2, the barrel of this second cylindrical barrel body 2 portion from top to bottom is disposed with second escape pipe 22, second input pipe 21, second drain pipe 23, and relative second cylindrical barrel body 2 of the second end 21b of this second input pipe 21 is tilted to down and is tangent with the sidewall of second cylindrical barrel body 2;
Described second cylindrical barrel body 2 is provided with a pair of liquid level gauge LIT;
Simultaneously, the port of export 22a of this second escape pipe 22 opens the side wall upper part at second cylindrical barrel body 2, the entrance point 22b of the 3rd escape pipe 22 extend into central authorities in the top of second cylindrical barrel body 2 from bottom to top, and, above the 3rd escape pipe 22 entrance point 22b, also be provided with a umbrella top cover 22c, between umbrella top cover 22c and entrance point 22b, be connected with support bar 22d.
Described stoste input pipe I is provided with straight up, and the first end 21a of its top and second input pipe 21 is connected, and the middle part of this second input pipe 21 then is connected with first input pipe 11.
As shown in Figure 4, described mist eliminator C is a spiral-flow type mist eliminator, this mist eliminator C comprises tank body 3, these tank body 3 tops are provided with that the 3rd escape pipe 32, sidewall are provided with the 3rd input pipe 31, the bottom is provided with the 3rd drain pipe 33, and second escape pipe 22 on described second cylindrical barrel body 2 is connected with the 3rd input pipe 31;
Simultaneously, the 3rd input pipe 31 is tangent with the sidewall of tank body 3, and described the 3rd escape pipe 32 extend into the central interior of tank body 3 from the top of tank body 3, the bottom 32a opening of the 3rd escape pipe 32 and as the inlet of the 3rd escape pipe 32, the bottom of tank body 3 is provided with a support 34, and the height of this support 34 is looked actual needs and adjusted.
Workflow is as follows:
The gas-liquid mixture that has certain pressure is input to this Separate System of Water-jet from stoste input pipe I, gas-liquid mixture is input to second input pipe 21 from bottom to top by stoste input pipe I, be arranged on second input pipe, 21 supermedial preseparator A, the pre-separation from gas-liquid mixture of liquid phase thing is come out;
Separate gas-liquid separation from the gas-liquid mixture of second input pipe, 21 tangential inputs by spiral-flow type gas-liquid separator B, gas is from 22 outputs of second escape pipe, and liquid is from 23 outputs of second drain pipe;
And tangentially enter in the mist eliminator B then from the gas phase thing of second escape pipe, 22 outputs, mist eliminator B catches the drop in the gas phase thing, and carries out further gas, liquid separation, and is last, the gas phase thing is from 32 outputs of the 3rd escape pipe, and drop compiles the back from 33 outputs of the 3rd drain pipe.
Claims (5)
1. a Separate System of Water-jet is characterized in that: comprise a stoste input pipe (I), a preseparator (A), a spiral-flow type gas-liquid separator (B) and a mist eliminator (C);
Wherein, described preseparator (A) comprises first cylindrical barrel body (1), the top of this first cylindrical barrel body (1) is provided with first input pipe (11), the bottom is provided with first drain pipe (12), and this first input pipe (11) while is as the outlet of the inlet and the gas of liquid;
Described spiral-flow type gas-liquid separator (B) comprises second cylindrical barrel body (2), the barrel of this second cylindrical barrel body (2) portion from top to bottom is disposed with second escape pipe (22), second input pipe (21), second drain pipe (23), and relative second cylindrical barrel body of second end (21b) (2) of this second input pipe (21) is tilted to down and is tangent with the sidewall of second cylindrical barrel body (2);
Described stoste input pipe (I) is provided with straight up, and first end (21a) of its top and second input pipe (21) is connected, and the middle part of this second input pipe (21) then is connected with first input pipe (11);
Described mist eliminator (C) comprises tank body (3), this tank body (3) top is provided with that the 3rd escape pipe (32), sidewall are provided with the 3rd input pipe (31), the bottom is provided with the 3rd drain pipe (33), and second escape pipe (22) on described second cylindrical barrel body (2) is connected with the 3rd input pipe (31).
2. gas-oil-water separation system according to claim 1, it is characterized in that: in described spiral-flow type gas-liquid separator (B), the port of export (22a) of this second escape pipe (22) is opened the side wall upper part in second cylindrical barrel body (2), the entrance point (22b) of the 3rd escape pipe (22) extend into central authorities in the top of second cylindrical barrel body (2) from bottom to top, and, also be provided with a umbrella top cover (22c) in the top of the 3rd escape pipe (22) entrance point (22b), between umbrella top cover (22c) and entrance point (22b), be connected with support bar (22d).
3. gas-oil-water separation system according to claim 1 is characterized in that: described second cylindrical barrel body (2) is provided with a pair of liquid level gauge (LIT).
4. according to claim 1 or 2 or 3 described gas-oil-water separation systems, it is characterized in that: described mist eliminator (C) is a spiral-flow type mist eliminator, the 3rd input pipe (31) is tangent with the sidewall of tank body (3), and described the 3rd escape pipe (32) extend into the central interior of tank body (3) from the top of tank body (3), bottom (32a) opening of the 3rd escape pipe (32) and as the inlet of the 3rd escape pipe (32).
5. gas-oil-water separation system according to claim 4 is characterized in that: the bottom of described mist eliminator (C) tank body (3) is provided with a support (34).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206158073U CN201959692U (en) | 2010-11-11 | 2010-11-11 | Gas-liquid separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206158073U CN201959692U (en) | 2010-11-11 | 2010-11-11 | Gas-liquid separation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201959692U true CN201959692U (en) | 2011-09-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010206158073U Expired - Lifetime CN201959692U (en) | 2010-11-11 | 2010-11-11 | Gas-liquid separation system |
Country Status (1)
| Country | Link |
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| CN (1) | CN201959692U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101972579A (en) * | 2010-11-11 | 2011-02-16 | 宁波威瑞泰默赛多相流仪器设备有限公司 | Gas-liquid separation system |
-
2010
- 2010-11-11 CN CN2010206158073U patent/CN201959692U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101972579A (en) * | 2010-11-11 | 2011-02-16 | 宁波威瑞泰默赛多相流仪器设备有限公司 | Gas-liquid separation system |
| CN101972579B (en) * | 2010-11-11 | 2013-10-02 | 宁波威瑞泰默赛多相流仪器设备有限公司 | Gas-liquid separation system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20110907 Effective date of abandoning: 20131002 |
|
| RGAV | Abandon patent right to avoid regrant |