CN202263488U - Axial-flow duct-type gas-liquid separator - Google Patents

Abstract

The utility model discloses an axial flow pipeline type gas-liquid separator. It includes a separator housing, and the position of the opposite two side walls of the separator housing is respectively provided with a gas-liquid mixture inlet pipeline and a gas outlet pipeline; the gas-liquid mixture inlet pipeline is composed of a circular platform cylinder a and The cylindrical body A arranged at the large-diameter end of the circular platform body a is composed of; the gas outlet pipeline is composed of the circular platform body b and the cylindrical body B respectively arranged at the small-diameter end and the large-diameter end of the circular platform body b It is composed of a cylinder body C; part of the cylinder body B is located in the cavity of the platform body a, and a ring cavity is formed between the platform body a and the cylinder body B; this The gas-liquid separator of the utility model has a compact overall structure and standard flanges at both ends, which is convenient for connection and disassembly with pipelines; the separator shell is used as a liquid collection chamber, eliminating the need for liquid storage equipment; the outlet pipe of the separator The expansion structure can reduce the loss of pressure energy.

Description

An axial flow pipeline type gas-liquid separator

technical field

The utility model relates to a gas-liquid separator, in particular to an axial flow pipeline type gas-liquid separator.

Background technique

During the process from production to consumption of natural gas, liquid water and heavy hydrocarbons often appear, which will reduce the circulation area of the pipeline, reduce the effective transmission capacity of the pipeline, increase the pressure drop of the pipeline, and even form hydrate, which will block the pipeline in serious cases; The acid gas gathering and transportation pipeline will also cause corrosion damage to the pipeline. Therefore, the natural gas must be dehydrated and dehydrocarbonized before long-distance pipeline safe transportation or light hydrocarbon recovery. Using gas-liquid separation equipment is an efficient and simple method .

At present, the gas-liquid separators commonly used in the petroleum industry at home and abroad are mainly centrifugal separators, and their main separation forces are centrifugal force, rotational power and impact force. Most conventional centrifugal gas-liquid separation technologies have the problem of gas overflow, and face the problems of low separation efficiency and excessive pressure drop. In recent years, the geographical particularity of offshore oil and gas fields and offshore platforms has put forward new requirements for gas-liquid separation technology and separators in oil and gas gathering and transportation: first, the structure of the separator must be compact to meet the stringent space requirements; secondly, There is a need to improve separation efficiency and reduce processing costs. Based on the above two points, the compact separator using the principle of centrifugal separation has become the first choice.

At present, the most common compact separators include cyclone separators, hydrocyclones, rotary power separators, online rotary separators, etc., but there are defects such as excessive pressure drop or complex structure, and easy failure of moving parts. Therefore, It is necessary to develop a compact separator with simple structure, convenient installation, small pressure drop and high separation efficiency.

Utility model content

The purpose of this utility model is to provide a gas-liquid separator with a compact structure. The gas-liquid separator has no moving parts and can be directly connected to a standard flange to reduce floor space, improve separation efficiency, and reduce pressure loss.

The utility model provides an axial flow pipeline type gas-liquid separator, which includes a separator shell, and the corresponding positions of the opposite two side walls of the separator shell are respectively provided with a gas-liquid mixture inlet pipeline and a gas-liquid mixture inlet pipeline. An outlet pipeline; the bottom of the separator housing is provided with a liquid outlet pipeline; the gas-liquid mixture inlet pipeline is composed of a circular platform cylinder a and a cylindrical cylinder A arranged at the large-diameter end of the circular platform cylinder a; The cylindrical shell A is opened outside the separator housing, and the circular table shell a is opened in the cavity of the separator shell; the gas outlet pipeline is respectively arranged on the circular table shell b and the circular table The small-diameter end and the large-diameter end of the cylinder b are composed of a cylindrical cylinder B and a cylindrical cylinder C; the cylindrical cylinder C is opened outside the separator shell, and the cylindrical cylinder B is opened in the separator shell In the cavity of the body; part of the cylindrical body B is located in the cavity of the cylindrical body a, and a ring cavity is formed between the cylindrical body a and the cylindrical body B; the gas The liquid mixture inlet pipeline and the cavity of the cylinder B are provided with a separator inner cone that is homogeneously free from the gas-liquid mixture inlet pipeline and the cylinder B, and the separator inner cone is composed of The frustum of a cone is composed of a cone arranged at the large-diameter end of the frustum of the cone; the cone is arranged in the cavity of the cylindrical body A; the cone is provided with a spiral inlet guide vane fixedly connected thereto , the outer edge of the spiral inlet guide vane is fixedly connected with the inner wall of the cylinder body A.

In the above-mentioned gas-liquid separator, the end faces of the cylinder body A end of the gas-liquid mixture inlet pipeline and the cylinder cylinder body C end of the gas outlet pipeline can be equal in diameter to the delivery pipeline, and are welded with standard flanges, which can be Quickly connect and disassemble with the delivery pipeline; the cavity between the separator housing and the gas-liquid mixture inlet pipeline and the gas outlet pipeline can be used as a liquid collection chamber instead of a liquid storage device.

In the above-mentioned gas-liquid separator, the taper of the frustum cylinder a and the frustum of the cone can be 5°-10°; the taper of the frustum cylinder a is equal to the taper of the frustum of the cone; The taper of the inner edge of the spiral inlet guide vane and the taper of the cone can be 60°-90°; the taper of the inner edge of the spiral inlet guide vane is equal to the taper of the cone; the cylinder The taper of the exhaust ring cavity formed by the body B and the frustum of the cone may be 30°-45°.

In the above-mentioned gas-liquid separator, the gas-liquid mixture inlet pipeline and the separator housing can pass through the depression provided on the gas-liquid mixture inlet pipeline and the boss provided on the separator housing Tight fit: the gas outlet pipeline and the separator housing can be closely matched through the depression provided on the gas outlet pipeline and the boss provided on the separator housing.

In the above-mentioned gas-liquid separator, the cylindrical body A is arranged outside the separator housing, and the circular platform body a is arranged in the cavity of the separator casing.

In the above-mentioned gas-liquid separator, the cylindrical body C is arranged outside the separator housing, and the circular table body b and the cylindrical body B are arranged in the cavity of the separator housing.

In the above-mentioned gas-liquid separator, the interface between the cylindrical cylinder A and the frustum a is coincident with the interface between the cone and the frustum a; the bottom surface of the small diameter end of the frustum coincides with the The interface between the cylinder body B and the frustum body b coincides.

In the above-mentioned gas-liquid separator, the inlet guide vanes are evenly distributed on the cone; the inlet guide vanes are welded together with the separator inner cone and the gas-liquid mixture inlet pipeline to form a The spiral tapered channel, through which the fluid generates high-speed rotational motion, provides the centrifugal force required for separation.

In the above-mentioned gas-liquid separator, the inlet guide vane, the cone and the cylinder A are all welded or riveted.

In the above-mentioned gas-liquid separator, the inner wall of the cylinder body B is provided with a support vane; the other side of the support vane and the inner cone of the separator pass through a fixed groove arranged on the inner cone of the separator. Tight fit; one function of the supporting vanes is to fix the inner cone of the separator, and the other function is to reduce the rotational strength of the separated gas and restore it to the axial flow.

In the above-mentioned gas-liquid separator, the liquid outlet pipeline is arranged at 2/3 of the axial length of the bottom of the separator shell, and the external valve of the liquid outlet pipeline can be controlled by a liquid level measurement facility, which can be safely Drain the liquid and keep the gas free.

The gas-liquid separator provided by the utility model has a compact overall structure and has standard flanges at both ends, which is convenient for connection and disassembly with pipelines; the combination of spiral blades and inner cones increases the rotational strength of the fluid, thereby improving Separation efficiency: the inner cone and inlet pipe with the same cone angle are used to form an annular separation area for high-speed rotating fluid to complete gas-liquid separation, and avoid gas overflow and reduce pressure drop; the separator shell is used as a liquid collection The cavity saves the liquid storage equipment; the outlet pipe of the separator adopts an expanded structure, which can reduce the loss of pressure energy.

Description of drawings

Figure 1 is a schematic structural view of the gas-liquid separator of the present invention.

Fig. 2 is a structural schematic diagram of the inlet guide vane and the inner cone of the separator of the gas-liquid separator of the present invention.

Detailed ways

The utility model will be further described below in conjunction with the accompanying drawings, but the utility model is not limited to the following embodiments.

The structure of the gas-liquid separator of the present utility model is shown in Figure 1, and each label in the figure is as follows: 1 separator shell, 2 gas-liquid mixture inlet pipeline, 3 inlet guide vane, 4 separator inner cone, 5 gas outlet Pipeline, 6 liquid outlet pipeline, 7 cylinder A, 8 cylinder a, 9 cylinder B, 10 cylinder b, 11 cylinder C, 12 cone, 13 cone, 14 supporting blade , 15 fixed slots, 16 standard flanges, 17 drain flanges.

The gas-liquid separator of the present utility model comprises a separator housing 1, a side wall of the separator housing 1 is provided with a gas-liquid mixture inlet pipeline 2, and the gas-liquid mixture inlet pipeline 2 is provided with a boss ( not shown in the figure), the side wall of the separator housing 1 is provided with a depression (not shown in the figure), and the gas-liquid mixture inlet pipeline 2 and the separator housing 1 are closely matched through the depression and the boss; the The gas-liquid mixture inlet pipeline 2 is composed of a circular platform cylinder a8 and a cylindrical cylinder A7 arranged at the large-diameter end of the circular platform cylinder a8; the cylindrical cylinder A7 is arranged outside the separator housing 1, and the circular platform cylinder a8 is arranged in the In the cavity of the device housing 1; a gas outlet pipeline 5 is provided at the position corresponding to the side wall opposite to the side wall provided with the gas-liquid mixture inlet pipeline 2, and a convex valve is provided on the gas outlet pipeline 5. platform (not shown in the figure), the side wall of the separator housing 1 is provided with a depression (not shown in the figure), and the gas outlet pipeline 5 and the separator housing 1 are closely matched through the depression and the boss; the The gas outlet pipeline 5 is composed of a cylindrical cylinder b10 and a cylindrical cylinder B9 and a cylindrical cylinder C11 respectively arranged at the small diameter end and the large diameter end of the cylindrical cylinder b10; the cylindrical cylinder B9 and the cylindrical cylinder b10 are arranged in the separator In the cavity of the housing 1, the cylindrical cylinder C11 is arranged outside the separator housing 1; part of the cylindrical cylinder B9 is located in the cavity of the round platform cylinder a8, and a liquid discharge ring cavity is formed between the two; the cylindrical cylinder The outer ends of the body A7 and the cylinder C11 are connected to the conveying pipeline with the same diameter through the standard flange 16, so as to realize quick installation and disassembly; The cavity between them can be used as a liquid collection chamber instead of a liquid storage device; the gas-liquid mixture inlet pipeline 2 and the cylinder body B9 are provided with a separation device that is free from the gas-liquid mixture inlet pipeline 2 and the cylinder body B9. Device inner cone 4, the separator inner cone 4 is made up of cone 12 and conical body 13, and cone 12 is arranged on the large diameter end of conical body 13; It coincides with the interface of the frustum cylinder a8, and the bottom surface of the small-diameter end of the cone cylinder 13 coincides with the interface between the cylinder B9 and the cone b10; the taper of the exhaust ring cavity formed by the cylinder B9 and the cone 13 is 30°, forming a flow channel with a gradually expanding section, which can expand the separated gas, reduce the speed, and reduce the pressure drop; the taper of the conical body 13 is equal to the taper of the conical body a8, both of which are 5°, and the two form a ring The separation area, so as to maintain and increase the rotational speed of the fluid and avoid the reverse flow of gas; the cone 12 is welded with evenly distributed spiral inlet guide vanes 3, the inner edge of the inlet guide vanes 3 and the cone 12 The tapers are equal, both are 60°, and the two form a spiral tapered channel, so that the gas-liquid mixture with separation is forced to change from axial flow to high-speed rotational flow; the outer edge of the inlet guide vane 3 is welded and fixed on the cylindrical tube On the inner wall of body A7; the gas-liquid mixture completes the separation process in the separation zone, and the separated liquid passes through the liquid discharge ring formed by the circular table body a8 and the cylindrical body B9 The separated gas enters the gas outlet pipeline 5 through the exhaust ring cavity; the inner wall of the cylinder B9 is welded with supporting blades 14, and the other side of the supporting blades 14 passes through the inner cone 4 of the separator. The fixed groove 15 on the top is closely matched with the inner cone 4 of the separator, and the supporting vane 14 can also weaken the rotational strength of the separated gas while supporting it, which is beneficial to the recovery of pressure energy; the liquid outlet pipeline 6 is arranged in the separator shell At 2/3 of the axial length of the bottom of the body 1, the lower end of the liquid outlet pipeline 6 is welded with a drain flange 17, the liquid outlet pipeline 6 communicates with the cavity of the separator housing 1, and the separated liquid flows from The liquid outlet line 6 discharges.

In the above-mentioned gas-liquid separator, the gas-liquid mixture inlet pipeline 2 and the gas outlet pipeline 5 can also be connected to the separator housing 1 by other means, such as welding or riveting; the inlet guide vane 3 can also be connected to the cone by other means. Body 12 and cylinder body A7 are fixedly connected, such as riveting; the inner edge of inlet guide vane 3 and the taper of cone 12 can be adjusted between 30°-60°; the taper of cone body a8 and cone body 13 can be It can be adjusted between 5°-10°; the taper of the exhaust ring cavity formed between the cylinder body B9 and the frustum of the cone 13 can be adjusted between 30°-45°.

When using the above gas-liquid separator of the present utility model, the gas-liquid mixture to be separated enters the gas-liquid mixture inlet pipeline 2, and then passes through the spiral tapered passage formed by the inlet guide vane 3 and the cone 12 of the separator inner cone 4 Finally, a high-speed rotating fluid is formed, and then enters the separation zone formed by the frustum cylinder a8 and the frustum 13; the liquid with higher density migrates to the outside of the separation zone under the action of the centrifugal force provided by the rotation motion, and enters the separation zone formed by the frustum cylinder a8 Gather at the inner wall of the liquid discharge ring cavity, and then enter the liquid collection cavity through the liquid discharge ring cavity, and finally discharge the gas-liquid separator through the liquid outlet pipeline 6; while the gas with a lower density rotates along the inner side of the separation zone, and finally reaches the exhaust ring cavity, and then enters into the conical cylinder b10 of the gas outlet pipeline 5 under the action of the “down-rotation” of the supporting blades 14, after the expansion of the conical cylinder b10, the separated gas recovers part of the pressure energy, and finally passes through the cylindrical cylinder C11 exits the accumulator.

Claims (10)

1. axial flow duct type gas-liquid separator, it comprises shell separator, the corresponding position, position of two sidewalls that said shell separator is relative is respectively equipped with gas-liquid mixture entrance pipe and gas export pipeline; The bottom of said shell separator is provided with the liquid outlet pipeline; It is characterized in that: said gas-liquid mixture entrance pipe is made up of round platform cylindrical shell a and the cylindrical tube A that is arranged at the heavy caliber end of said round platform cylindrical shell a; Said cylindrical tube A is opened on outside the said shell separator, and said round platform cylindrical shell a is opened in the cavity of said shell separator; Said gas outlet tube route round platform cylindrical shell b and the cylindrical tube B and the cylindrical tube C that are arranged at small-caliber end and the heavy caliber end of said round platform cylindrical shell b respectively form; Said cylindrical tube C is opened on outside the said shell separator, and said cylindrical tube B is opened in the cavity of said shell separator; The part cylindrical shell of said cylindrical tube B is positioned at the cavity of said round platform cylindrical shell a, and forms a ring cavity between said round platform cylindrical shell a and the said cylindrical tube B; Be provided with in the said gas-liquid mixture entrance pipe and in the cavity of said cylindrical tube B and said gas-liquid mixture entrance pipe and the free separator inner cone of said cylindrical tube B homogeneous phase, said separator inner cone is made up of Rotary-table and the cone that is arranged at the heavy caliber end of said Rotary-table; Said cone is located in the cavity of said cylindrical tube A; Said cone is provided with the spirality inlet guide vane that is fixedly connected with it, and the outer rim of said spirality inlet guide vane is fixedly connected with the inwall of said cylindrical tube A.

2. gas-liquid separator according to claim 1 is characterized in that: the tapering of said round platform cylindrical shell a and the tapering of said Rotary-table are 5 °-10 °; The tapering of said round platform cylindrical shell a equates with the tapering of said Rotary-table; The tapering of said spirality inlet guide vane inner edge and the tapering of said cone are 60 °-90 °; The tapering of said spirality inlet guide vane inner edge equates with the tapering of said cone; The tapering of the exhaust ring cavity that said cylindrical tube B and said Rotary-table form is 30 °-45 °.

3. gas-liquid separator according to claim 1 and 2 is characterized in that: said gas-liquid mixture entrance pipe and said shell separator closely cooperate through the boss that is arranged at the depression on the said gas-liquid mixture entrance pipe and be arranged on the said shell separator; Said gas vent pipeline and said shell separator closely cooperate through the boss that is arranged at the depression on the said gas vent pipeline and be arranged on the said shell separator.

4. gas-liquid separator according to claim 1 and 2 is characterized in that: said cylindrical tube A is located at outside the said shell separator, and said round platform cylindrical shell a is located in the cavity of said shell separator.

5. gas-liquid separator according to claim 1 and 2 is characterized in that: said cylindrical tube C is located at outside the said shell separator, and said round platform cylindrical shell b and cylindrical tube B are located in the cavity of said shell separator.

6. gas-liquid separator according to claim 1 and 2 is characterized in that: the interface of said cylindrical tube A and said round platform cylindrical shell a overlaps with the interface of said cone and said Rotary-table; The bottom surface of the small-caliber end of said Rotary-table overlaps with the interface of said cylindrical tube B and said round platform cylindrical shell b.

7. gas-liquid separator according to claim 1 and 2 is characterized in that: said spirality inlet guide vane is uniformly distributed on the said cone.

8. gas-liquid separator according to claim 1 and 2 is characterized in that: be welding or riveted joint between said spirality inlet guide vane and said cone and the said cylindrical tube A.

9. gas-liquid separator according to claim 1 and 2 is characterized in that: the inwall of said cylindrical tube B is provided with support blade; The opposite side of said support blade and said separator inner cone closely cooperate through the holddown groove that is arranged on the said separator inner cone.

10. gas-liquid separator according to claim 1 and 2 is characterized in that: said liquid outlet pipeline is arranged at 2/3 place of the axial length of said shell separator bottom.

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