CN210495691U - Gas-liquid separation tank - Google Patents
Gas-liquid separation tank Download PDFInfo
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- CN210495691U CN210495691U CN201921059111.4U CN201921059111U CN210495691U CN 210495691 U CN210495691 U CN 210495691U CN 201921059111 U CN201921059111 U CN 201921059111U CN 210495691 U CN210495691 U CN 210495691U
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Abstract
The utility model provides a gas-liquid separation jar, when it carries out the partition to gas-liquid separation jar through utilizing the liquid level division board, set up the overflow pipe on gas-liquid separation jar, fluid infusion pipe and level gauge, measure the working liquid level in the second jar body partition intracavity through the level gauge, after the working liquid in gas-liquid separation jar is discharged to pump body starting pressure, when the liquid level is close the circulation mouth, carry out the fluid infusion through the fluid infusion pipe, avoid gas leakage, in the current gas-liquid separation jar use has been solved, the technical problem that the working liquid leads to gas leakage is extruded to pump body starting pressure.
Description
Technical Field
The utility model relates to a gas-liquid separation equipment technical field specifically is a gas-liquid separation jar.
Background
In the gas-liquid phase separation occasions, such as steam recovery, tail gas treatment and other working environments, especially in the working environment of back pumping flammable, explosive, toxic and other gases, the gas must be sent to a specified pipeline, and absolutely no leakage and discharge are allowed to be carried out in other pipelines. If the water leaks or is discharged into other pipelines, economic losses are caused, and the safety of lives and properties is endangered and safety accidents are caused. And because the pump body needs to be subjected to isothermal compression in the working environment and needs to be pumped out, the working fluid needs to absorb heat generated by gas compression in the process of vacuumizing and compressing the gas, so that the temperature of the working fluid is increased. If the completely circulated working fluid is not cooled, the temperature is higher and higher, the high temperature of the working fluid can affect the vacuum degree of the pump body on one hand, and can cause the cavitation phenomenon of the pump body to cause the damage of the pump body on the other hand.
However, in the gas-liquid separation tank used in the conventional pump body, during the gas-liquid separation process, the working fluid is discharged from the gas-liquid separation tank due to the instantaneous pressure of the liquid ring pump during the starting process, so that the liquid level of the working fluid is lower than the overflow inlet of the overflow pipe, and gas leakage occurs.
Patent No. 201320678959.1 discloses an ejector flow stopping device, including the separator casing, be equipped with at the top of separator casing and draw and penetrate the gas outlet, be equipped with on the lateral wall of separator casing upper portion and draw and penetrate gas inlet, be equipped with the gas-liquid separation room in separator casing inner chamber, the below of drawing and penetrating gas inlet, the liquid inlet channel intercommunication is passed through with separator casing inner chamber top to gas-liquid separation room bottom, and gas-liquid separation room upper portion is equipped with the overflow pipe that extends the separator casing outside.
Although the above patent discloses separating the separator tank housing by a transverse partition and a vertical partition, it does not solve the technical problem of the discharge of the working fluid caused by the pressure of the instantaneous actuation of the pump body.
SUMMERY OF THE UTILITY MODEL
To above problem, the utility model provides a gas-liquid separation jar, when it carries out the partition to gas-liquid separation jar through utilizing the liquid level division board, set up the overflow pipe on gas-liquid separation jar, fluid infusion pipe and level gauge, through the working solution level of level gauge second jar body partition intracavity, after the working solution discharge in pump body starting pressure is with gas-liquid separation jar, when the liquid level is close to the circulation mouth, carry out the fluid infusion through the fluid infusion pipe, avoid gas leakage, in the current gas-liquid separation jar use has been solved, by pump body starting pressure extrusion working solution lead to gas leakage's technical problem.
In order to achieve the above object, the utility model provides a following technical scheme:
a gas-liquid separation tank comprising:
the gas-liquid separation tank is vertically arranged, an inverted L-shaped liquid level partition plate is arranged in the gas-liquid separation tank, the gas-liquid separation tank is separated by the liquid level partition plate to form a first tank body separation cavity and a second tank body separation cavity, and the first tank body separation cavity is positioned above the second tank body separation cavity;
a circulation port for communicating the first tank body separation cavity and the second tank body separation cavity is arranged between the liquid level partition plate and the bottom plate of the gas-liquid separation tank, and a tank body exhaust port for exhausting gas is arranged at the top of the first tank body separation cavity;
the top of the first tank body separation cavity is communicated with an air outlet on an external pump body through an air exhaust pipeline, and the lower part of the second tank body separation cavity is communicated with a working liquid inlet on the pump body through a return pipeline, so that the pump body and working liquid in the gas-liquid separation tank circularly flow;
a liquid supplementing pipe is arranged on the second tank body separation cavity, and a liquid supplementing valve for controlling the switch is arranged on the liquid supplementing pipe;
an overflow pipe is arranged on the second tank body separation cavity, and the connection position of the overflow pipe and the second tank body separation cavity is positioned at the upper part of the second tank body separation cavity;
one side that the second jar body separates the chamber is provided with the level gauge, and this level gauge is vertical to be set up, its upper end and lower extreme equally divide respectively with the second jar body separates the chamber intercommunication.
As an improvement, when the pump body is started, the working fluid in the first tank compartment is pressed into the second tank compartment through the flow port.
As a refinement, the first tank compartment has a volume of V1, the second tank compartment has a volume of V2, and the relationship between V1 and V2 is satisfied: v1 < V2.
As an improvement, the height of the flow opening from the bottom plate of the gas-liquid separation tank is 2-3 cm.
As an improvement, the height of the working liquid level in the first tank partition cavity is higher than that of the circulating port.
As an improvement, the part of the overflow pipe, which is positioned in the second tank compartment, is in an inverted L shape, and the part of the overflow pipe comprises a horizontal pipeline and a vertical pipeline, wherein the horizontal pipeline is horizontally arranged, the vertical pipeline is vertically arranged, and an overflow inlet at the lower part of the vertical pipeline is positioned below the working liquid level in the second tank compartment.
As an improvement, an emptying pipeline is arranged at the bottom of the second tank separation cavity, an emptying valve which is opened and closed by a controller is arranged on the emptying pipeline, and the part of the emptying pipeline, which is positioned at the rear side of the emptying valve, is communicated with the overflow pipe along the flowing direction of the emptying pipeline.
As an improvement, a guide inclined plate is arranged at the flow opening and obliquely and downwards points to the second tank body separation cavity.
The beneficial effects of the utility model reside in that:
(1) the utility model discloses a when utilizing the liquid level division board to separate the gas-liquid separation jar, set up overflow pipe, fluid infusion pipe and level gauge on the gas-liquid separation jar, measure the working liquid level in the second jar body partition cavity through the level gauge, after pump body starting pressure discharges the working liquid in the gas-liquid separation jar, when the liquid level is close the circulation mouth, carry out the fluid infusion through the fluid infusion pipe, avoid gas leakage, solved current gas-liquid separation jar in the use, by pump body starting pressure extrusion working liquid lead to the technical problem of gas leakage;
(2) the overflow pipe is arranged on the separate cavity of the second tank body, and the whole-process liquid seal of the overflow port of the gas-liquid separation tank is realized through the arrangement of the overflow pipe, so that the overflow pipe port is always below the liquid level, the toxic and harmful process gas is prevented from leaking or flowing to other pipelines from the overflow port, the measure can stop the occurrence of potential hazard, and the production environment is safer;
(3) the utility model discloses a direction swash plate that sets up the slope in circulation mouth department leads to the working solution that the first jar of body separates the intracavity, makes the smooth and easy water conservancy diversion of the working solution that the first jar of body separates the intracavity separate the intracavity to the second jar of body, makes the dust that enters into the first jar of body and separate the intracavity can not pile up in it.
To sum up, the utility model has the advantages of sealed effectual, gas-liquid separation is thorough, is particularly useful for gas-liquid separation equipment technical field.
Drawings
FIG. 1 is a schematic perspective view of the present invention;
FIG. 2 is a schematic view of a partial structure of the present invention;
fig. 3 is a schematic sectional view of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and to simplify the description, but do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore should not be construed as limiting the present invention.
Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless specifically limited otherwise.
Example 1:
as shown in fig. 1 to 3, a gas-liquid separation tank includes:
the gas-liquid separation tank 2 is vertically arranged, an inverted L-shaped liquid level partition plate 21 is arranged in the gas-liquid separation tank 2, the gas-liquid separation tank 2 is separated by the liquid level partition plate 21 to form a first tank body separation cavity 22 and a second tank body separation cavity 23, and the first tank body separation cavity 22 is positioned above the second tank body separation cavity 23;
a circulation port 24 for communicating the first tank compartment 22 with the second tank compartment 23 is arranged between the liquid level partition plate 21 and the bottom plate of the gas-liquid separation tank 2, and a tank exhaust port 221 for exhausting gas is arranged at the top of the first tank compartment 22;
the top of the first tank separation chamber 22 is communicated with an exhaust port on an external pump body through an exhaust pipeline 25, and the lower part of the second tank separation chamber 23 is communicated with a working liquid inlet on the pump body through a return pipeline 26, so that the pump body and the working liquid in the gas-liquid separation tank 2 circularly flow, wherein the pump body in the invention is preferably a liquid ring pump 1, an exhaust port 11 on the liquid ring pump 1 is communicated with the first tank separation chamber 23, and a working liquid inlet 12 on the liquid ring pump 1 is communicated with the second tank separation chamber 24, but it should be emphasized that the gas-liquid separation cooling system is not limited to be used in cooperation with the liquid ring pump, a screw pump and the like, and the gas-liquid separation cooling system can be used in any occasions requiring gas-liquid phase separation and liquid phase cooling, such as steam recovery, tail gas treatment and the like;
a liquid supplementing pipe 27 is arranged on the second tank body separation cavity 23, and a liquid supplementing valve 271 for controlling the switch is arranged on the liquid supplementing pipe 27;
an overflow pipe 28 is arranged on the second tank compartment 23, and the connection position of the overflow pipe 28 and the second tank compartment 23 is positioned at the upper part of the second tank compartment 23;
one side that the second jar body separates chamber 23 is provided with level gauge 3, and this level gauge 3 vertical setting, its upper end and lower extreme equally divide respectively with the second jar body separates chamber 23 intercommunication.
Further, when the liquid ring pump 1 is started, the working fluid in the first tank compartment 22 is pressed into the second tank compartment 23 through the communication port 24.
The gas discharge port 11 of the liquid ring pump is connected to the gas-liquid separation tank 2, the system gas discharge port is provided at the upper part of the gas-liquid separation tank 2, the gas from the gas discharge port 11 of the liquid ring pump is discharged from the tank body gas discharge port 221, and is collected and treated by the gas collecting device, and the liquid from the gas discharge port 11 of the liquid ring pump is left in the gas-liquid separation tank 2. An inverted L-shaped liquid level separation plate 21 is welded in the gas-liquid separation tank 2, the liquid level separation plate 21 and the pipe wall of the gas-liquid separation tank 2 are fully welded, and a circulation opening 24 with the diameter of about 2 centimeters is formed in the bottom of the liquid level separation plate 21 and the bottom of the gas-liquid separation tank 2 to ensure that working liquid can circulate. Liquid level division board 21 can be cut apart into two independent cavitys with gas-liquid separation jar 2 inner space when working solution is higher than liquid level division board 21 lower part in gas-liquid separation jar 2, install overflow pipe 28 on gas-liquid separation jar 2, overflow pipe 28's one end need submerge in the below working solution level the other end and set up in gas-liquid separation jar 2 outside, the main function is isolated gas-liquid separation jar 2 air outflow and can follow overflow pipe 28 when the liquid level in gas-liquid separation jar 2 is higher than overflow pipe 28 upper end and discharge, prevent that the too high liquid ring pump 1 that arouses of working solution level from overloading in gas-liquid separation jar 2. The middle part of the gas-liquid separation tank 2 is provided with a water replenishing valve 27 and a liquid level meter 3, the liquid level meter 3 is provided with a liquid level switch or a liquid level transmitter, and the liquid level state can be monitored by matching with an electric control system, and automatic liquid replenishing is realized when the liquid level is too low. The lower part of the gas-liquid separation tank 2 is provided with a return pipeline 26, and the return pipeline 26 is connected with the working liquid inlet 12 of the liquid ring pump 1, so that the working liquid can be recycled.
Further, the first tank compartment 22 has a volume of V1, the second tank compartment 23 has a volume of V2, and V1 and V2 satisfy the following relationships: v1 < V2.
Further, the height of the circulation port 24 from the bottom plate of the gas-liquid separation tank 2 is 2 to 3cm, preferably 2 cm.
It should be noted that the operating fluid level in the first tank compartment 22 is higher than the level of the communication port 24.
As shown in FIG. 3, as a preferred embodiment, the portion of the overflow pipe 28 located within the second tank compartment 23 is an inverted L-shape that includes a horizontally disposed horizontal duct 281 and a vertically disposed vertical duct 282, wherein an overflow inlet 283 in the lower portion of the vertical duct 282 is located below the operating liquid level within the second tank compartment 22.
In the initial state, the liquid level in the gas-liquid separation tank 2 (the liquid level in the first tank compartment 22 is consistent with that in the second tank compartment 23) is positioned at the central line of the driving shaft of the liquid ring pump 1 (namely, at the middle position from the lower end of the liquid level division plate 21 to the upper end of the overflow pipe 28). When the liquid ring pump 1 is started, the gas passing through the gas outlet 11 of the liquid ring pump generates a certain positive pressure to the first tank compartment 22 in the gas-liquid separation tank 2, so that the liquid level in the first tank compartment 22 drops by a certain height, and the liquid level drop caused by the pressure must ensure that the liquid level is always higher than the lower end of the liquid level division plate, otherwise the gas intercommunication working liquid in the first tank compartment 22 and the second tank compartment 23 is left from the overflow pipe 28, so that the liquid level in the second tank compartment 23 drops to the height consistent with the liquid level in the first tank compartment 22, and the overflow pipe 28 loses the liquid sealing effect. Since the vertical portion of level divider 21 divides the liquid in the tank into a portion that is within first tank compartment 22 and a portion that is much smaller than the area within second tank compartment 23. For this reason, when the height of the liquid level 1 changes, the influence on the liquid level 2 is small, so that the bottom of the overflow pipe is always below the liquid level 2, namely, the liquid seal state is always realized, and the gas in the tank cannot flow out of the overflow pipe.
If no liquid level partition plate is arranged, when the liquid ring pump is started, the pressure in the pipe can press the working liquid out of the tank from the bottom of the overflow pipe. If the bottom of the overflow pipe is still below the liquid level, the liquid level in the tank is too low to meet the working requirement of the liquid ring pump, and the liquid ring pump is damaged; if the bottom of the overflow pipe is assumed to be level with the liquid level, gas in the tank flows out of the tank from the bottom of the overflow pipe due to consumption of working liquid and fluctuation of the liquid level during working, so that potential hazard of liquid seal cannot be realized, and the production environment is unsafe.
As shown in fig. 3, as a preferred embodiment, the bottom of the second tank compartment 23 is provided with an evacuation line 29, the evacuation line 29 is provided with an evacuation valve 291 which is controlled by a controller to open and close, and a portion of the evacuation line 29 located at the rear side of the evacuation valve 291 is communicated with the overflow pipe 28, so that the working fluid can be completely evacuated when impurities need to be discharged or maintenance needs to be performed.
As shown in fig. 3, as a preferred embodiment, a guiding inclined plate 4 is arranged at the communication port 24, and the guiding inclined plate 4 is obliquely and downwards directed to the second tank compartment 23.
It should be noted that when the liquid ring pump 1 is used to pump dust, the inclined guide plate 4 can guide the dust in the first tank compartment 22 into the second tank compartment 23, so as to prevent the dust from concentrating at the bottom of the first tank compartment 22.
The working process is as follows:
when the liquid ring pump 1 is started, the gas passing through the gas outlet 11 of the liquid ring pump generates a certain positive pressure to the first tank compartment 22 in the gas-liquid separation tank 2, so that the liquid level in the first tank compartment 22 drops by a certain height, and the liquid level drop caused by the pressure must ensure that the liquid level is always higher than the lower end of the liquid level division plate, otherwise the gas intercommunication working liquid in the first tank compartment 22 and the second tank compartment 23 is left from the overflow pipe 28, so that the liquid level in the second tank compartment 23 drops to the height consistent with the liquid level in the first tank compartment 22, and the overflow pipe 28 loses the liquid sealing effect. Since the vertical portion of level divider 21 divides the liquid in the tank into a portion that is within first tank compartment 22 and a portion that is much smaller than the area within second tank compartment 23. For this reason, when the height of the liquid level 1 changes, the influence on the liquid level 2 is small, so that the bottom of the overflow pipe is always below the liquid level 2, namely, the liquid seal state is always realized, and the gas in the tank cannot flow out of the overflow pipe.
The above description is only exemplary of the present invention and should not be taken as limiting the scope of the present invention, as any modifications, equivalents, improvements and the like made within the spirit and principles of the present invention are intended to be included within the scope of the present invention.
Claims (8)
1. A gas-liquid separation tank, comprising:
the gas-liquid separation tank (2) is vertically arranged, an inverted L-shaped liquid level partition plate (21) is arranged in the gas-liquid separation tank (2), the gas-liquid separation tank (2) is separated by the liquid level partition plate (21) to form a first tank body separation cavity (22) and a second tank body separation cavity (23), and the first tank body separation cavity (22) is positioned above the second tank body separation cavity (23);
a circulation port (24) for communicating a first tank body separation cavity (22) with a second tank body separation cavity (23) is arranged between the liquid level partition plate (21) and a bottom plate of the gas-liquid separation tank (2), and a tank body exhaust port (221) for exhausting gas is arranged at the top of the first tank body separation cavity (22);
the top of the first tank separation cavity (22) is communicated with an external exhaust port on the pump body through an exhaust pipeline (25), and the lower part of the second tank separation cavity (23) is communicated with a working liquid inlet on the pump body through a return pipeline (26), so that the pump body and the working liquid in the gas-liquid separation tank (2) circularly flow;
a liquid supplementing pipe (27) is arranged on the second tank body separation cavity (23), and a liquid supplementing valve (271) for controlling the switch is arranged on the liquid supplementing pipe (27);
an overflow pipe (28) is arranged on the second tank body compartment (23), and the connection position of the overflow pipe (28) and the second tank body compartment (23) is positioned at the upper part of the second tank body compartment (23);
one side that second jar body separates chamber (23) is provided with level gauge (3), and this level gauge (3) vertical setting, its upper end and lower extreme equally divide respectively with second jar body separates chamber (23) intercommunication.
2. A gas-liquid separation tank according to claim 1, characterized in that the operating fluid in said first tank compartment (22) is forced into said second tank compartment (23) through said through-flow opening (24) when the pump body is activated.
3. A knock tank according to claim 1, wherein the first tank compartment (22) has a volume V1 and the second tank compartment (23) has a volume V2, V1 and V2 which satisfy the relationship: v1 < V2.
4. A gas-liquid separation tank according to claim 1, characterized in that the height of the circulation port (24) from the bottom plate of the gas-liquid separation tank (2) is 2-3 cm.
5. A knock tank according to claim 1 wherein the level of the operating liquid in the first tank compartment (22) is higher than the level of the communication port (24).
6. A gas-liquid separation tank according to claim 1, characterized in that the part of the overflow pipe (28) located inside the second tank compartment (23) is inverted L-shaped and comprises a horizontally arranged horizontal duct (281) and a vertically arranged vertical duct (282), wherein the overflow inlet (283) at the lower part of the vertical duct (282) is located below the working liquid level in the second tank compartment (23).
7. A gas-liquid separation tank according to claim 1, characterized in that the bottom of the second tank compartment (23) is provided with an evacuation line (29), the evacuation line (29) is provided with an evacuation valve (291) which is controlled by a controller to be opened and closed, and the portion of the evacuation line (29) located at the rear side of the evacuation valve (291) is communicated with the overflow pipe (28) in the flow direction of the evacuation line (291).
8. A gas-liquid separation tank according to claim 1, characterized in that a sloping guide plate (4) is arranged at the through-flow opening (24), which sloping guide plate (4) is directed obliquely downwards towards the second tank compartment (23).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921059111.4U CN210495691U (en) | 2019-07-09 | 2019-07-09 | Gas-liquid separation tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921059111.4U CN210495691U (en) | 2019-07-09 | 2019-07-09 | Gas-liquid separation tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210495691U true CN210495691U (en) | 2020-05-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921059111.4U Active CN210495691U (en) | 2019-07-09 | 2019-07-09 | Gas-liquid separation tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210495691U (en) |
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2019
- 2019-07-09 CN CN201921059111.4U patent/CN210495691U/en active Active
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