CN212819000U - Contain sour gas unloading desulphurization unit - Google Patents
Contain sour gas unloading desulphurization unit Download PDFInfo
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- CN212819000U CN212819000U CN202020953981.2U CN202020953981U CN212819000U CN 212819000 U CN212819000 U CN 212819000U CN 202020953981 U CN202020953981 U CN 202020953981U CN 212819000 U CN212819000 U CN 212819000U
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- desulfurization
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- sulfur
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Abstract
The utility model is suitable for the technical field of chemical equipment, and provides a sulfur-containing gas emptying and desulfurizing device, which comprises a separator, a storage device and a plurality of desulfurizing areas, wherein the separator is used for removing liquid drops carried in emptying gas, the storage device is used for storing a desulfurizing agent, and the desulfurizing areas are used for desulfurizing the emptying gas; and gas distributors are arranged in the storage device and the desulfurization area. Therefore, the utility model can fully absorb the hydrogen sulfide in the vent gas, improve the desulfurization effect of the vent gas and improve the quality of the surrounding environment of the oil field; the whole device is of a skid-mounted structure, the manufacturing cost of equipment is low, the flow of the discharged air in the device is smooth and unobstructed, the safety is high, the desulfurizer is recycled, and the production cost is reduced.
Description
Technical Field
The utility model relates to a chemical industry equipment technical field especially relates to a contain gas unloading desulphurization unit.
Background
At present, the gas in the safety valve emptying during abnormal production of a crude oil processing station or temporary emptying equipment and a pipeline during maintenance can generate certain adverse effect on the surrounding environment. In many old oil fields with low sulfur content, the sulfur content is gradually increased in the later development stage, the hydrogen sulfide content in associated gas is increased year by year, and the sulfur content is more than 20mg/Nm3And the direct discharge threatens the health of operators and peripheral personnel of a crude oil station and pollutes the environment.
At the present stage, the country pays great attention to the environmental protection around the oil field, and does not allow the oil field station to discharge harmful gas containing hydrogen sulfide, and the production enterprises have to process the emptying gas of the crude oil processing station. Generally, the crude oil treatment station of the oil field can adopt a torch to discharge, when a torch system detects that gas needs to be discharged in a discharge pipeline, the discharge gas containing hydrogen sulfide is automatically ignited, and the gas is directly discharged after being burned by the torch. The method for discharging sulfur-containing gas by using the torch combustion has the advantages that the occupied area is small, the equipment investment is high, the operation is difficult when the torch is ignited by detecting the emptying gas, the torch is provided with the pilot burner and the ignited torch is easy to cause panic to surrounding residents, and the sulfur dioxide generated by combustion still pollutes the environment.
In view of the above, the prior art is obviously inconvenient and disadvantageous in practical use, and needs to be improved.
SUMMERY OF THE UTILITY MODEL
Aiming at the defects, the utility model aims to provide a sulfur-containing gas emptying and desulfurizing device which can fully absorb hydrogen sulfide in the emptying gas, improve the desulfurizing effect of the emptying gas and improve the quality of the surrounding environment of an oil field; the whole device is of a skid-mounted structure, the manufacturing cost of equipment is low, the flow of the discharged air in the device is smooth and unobstructed, the safety is high, the desulfurizer is recycled, and the production cost is reduced.
In order to achieve the aim, the utility model provides a sulfur-containing gas emptying and desulfurizing device, which comprises a separator, a storage device and a plurality of desulfurizing areas, wherein the separator is used for removing liquid drops carried in emptying gas, the storage device is used for containing a desulfurizing agent, and the desulfurizing areas are used for desulfurizing the emptying gas; and gas distributors are arranged in the storage device and the desulfurization area.
The storage device is respectively connected with a plurality of inlet valves of the desulfurization areas, and the outlet valve of each desulfurization area is connected with the storage device.
And partition plates are arranged between the separator and the storage device, between the storage device and the desulfurization area and between two adjacent desulfurization areas.
The gas distributor comprises an inverted U-shaped gas rising pipe, the bottom of the gas rising pipe is inserted below the partition plate, and the top of the gas rising pipe is communicated with the spray plate; the spray plate comprises a vertical main pipe and a transverse main pipe which are communicated with each other, the top end of the vertical main pipe is communicated with the top of the gas lift pipe, the transverse main pipe is communicated with a plurality of branch pipes, and the branch pipes are provided with a plurality of spray holes; the transverse main pipe and the branch pipes are both positioned below the liquid level of the desulfurizer.
According to the utility model discloses a contain sour gas unloading desulphurization unit, the separator is equipped with air inlet line and blowdown pipeline, the inside of separator is equipped with a plurality of liquid baffle plates.
According to the utility model discloses a contain gas unloading desulphurization unit, the outside of separator is equipped with and is used for real-time supervision the first level gauge of liquid level height in the separator.
According to the utility model discloses a sulfur-containing gas unloading desulphurization unit, the fender liquid board has 10 ~ 45 degrees contained angles with the horizontal plane.
According to the utility model discloses a contain gas unloading desulphurization unit, the ware is connected to the storage barren liquor input valve and rich liquid output valve, the bypass valve is still connected to the storage ware.
According to the utility model discloses a contain gas unloading desulphurization unit, still be equipped with on the storage device and be used for the monitoring the second level gauge of the liquid level height of desulfurizer in the storage device.
According to the utility model discloses a contain gas unloading desulphurization unit, the storage device with the outside in desulfurization district all is equipped with the manhole.
According to the utility model discloses a contain gas unloading desulphurization unit, the orifice is located the bottom of branch pipe, the aperture of orifice is 4 ~ 8 mm.
According to the utility model discloses a sulfur-containing gas unloading desulphurization unit, the top of device is equipped with the defoaming silk screen, the defoaming silk screen is equipped with 15 ~ 35 layers.
The utility model aims to provide a sulfur-containing gas emptying and desulfurizing device, which is characterized in that a separator, a storage device and a plurality of desulfurizing areas are arranged in sequence from bottom to top, the separator can remove liquid drops carried in emptying gas, the storage device is used for containing a desulfurizing agent and pouring the desulfurizing agent into each desulfurizing area arranged on the upper part of the storage device; gas distributors are arranged in the storage device and the desulfurization area; the gas distributor comprises an inverted U-shaped gas riser, the top of the gas riser is communicated with the vertical main pipe of the spray plate, the horizontal main pipe of the spray plate is communicated with a plurality of branch pipes, and the branch pipes are provided with a plurality of spray holes; the transverse main pipe and the branch pipes are both positioned below the liquid level of the desulfurizer, the discharged air without liquid drops enters the gas distributor in the storage device, hydrogen sulfide is absorbed for the first time in the storage device, then continuously enters the gas distributor in each desulfurization area upwards, and hydrogen sulfide is absorbed for multiple times, so that the content of hydrogen sulfide is lower than 20mg/Nm3. To sum up, the beneficial effects of the utility model are that: the hydrogen sulfide in the exhausted gas can be fully absorbed, the desulfurization effect of the exhausted gas is improved, and the quality of the surrounding environment of the oil field is improved; the whole device is of a skid-mounted structure, the manufacturing cost of equipment is low, the flow of the discharged air in the device is smooth and unobstructed, the safety is high, the desulfurizer is recycled, and the production cost is reduced.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a schematic diagram of the structure of the nozzle plate of the present invention;
FIG. 3 is a schematic view of the structure of FIG. 2 taken along line A-A;
in the figure: 1-separator, 2-blowdown pipeline, 3-air inlet pipeline, 4-barren liquor input valve, 5-bypass valve, 6-rich liquor output valve, 7-pump body outlet valve, 8-pump body, 9-first pump body inlet valve, 10-second pump body inlet valve, 11-spray plate, 111-vertical main pipe, 112-horizontal main pipe, 113-branch pipe and 114-spray hole; 12-partition board, 13-liquid baffle board, 14-first liquid level meter, 15-storage device, 16-second liquid level meter, 17-riser, 18-first desulfurization area inlet valve, 19-first desulfurization area outlet valve, 20-second desulfurization area inlet valve, 21-second desulfurization area outlet valve, 22-third desulfurization area inlet valve, 23-third desulfurization area outlet valve, 24-fourth desulfurization area inlet valve, 25-fourth desulfurization area outlet valve, 26-manhole, 27-defoaming screen and 28-gas outlet.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Referring to fig. 1, the utility model provides a contain gas unloading desulphurization unit, include detach drop separator 1, be used for holding the storage device 15 of desulfurizer and be used for a plurality of desulfurization district for the desulfurization of blow-down secretly in the blow-down. Gas distributors are arranged in the storage device 15 and the desulfurization area.
The separator 1 is located the bottommost of device, is equipped with air inlet pipeline 3 and sewage pipes 2 on the separator 1, and the inside of separator 1 is equipped with a plurality of liquid baffle 13, and liquid baffle 13 has 10 ~ 45 degrees contained angles with the horizontal plane. After the vent gas enters the separator 1 through the gas inlet pipeline 3, because the vent gas has certain pressure in the entering process, in the rising process, the vent gas and liquid drops carried by the vent gas collide with the liquid baffle 13, the liquid drops fall to the bottom of the separator 1 under the action of gravity, and the vent gas continues rising, thereby achieving the effect of gas-liquid separation. After long-term accumulation of liquid drops at the bottom of the separator 1, the liquid drops can be discharged through a sewage pipeline 2 and discharged to a sewage pipe network of a crude oil station. If the included angle between the liquid baffle plates 13 and the horizontal plane is less than 10 degrees, the gas channel formed between the liquid baffle plates 13 is too small, the rising speed of the discharged air is slow, and the separation efficiency is influenced; if the included angle between the liquid baffle 13 and the horizontal plane is more than 45 degrees, the gas channel formed between the liquid baffle 13 is too large, a large amount of emptying gas does not directly rise through the liquid baffle 13, the liquid drops are not separated thoroughly, and the separation effect is influenced. As a preferred scheme, a first liquid level meter 14 is further arranged outside the separator 1, the first liquid level meter 14 can monitor the liquid level height in the separator 1 in real time, liquid at the bottom of the separator 1 is discharged in time, and the influence on the separation of the vent gas is avoided. In the utility model, the diameter of the residual liquid drops in the discharged air is not more than 100 μm after the separation of the separator 1.
The storage device 15 is positioned at the upper part of the separator 1, the storage device 15 is connected with the lean liquid input valve 4 and the rich liquid output valve 6, the storage device 15 is respectively connected with the inlet valves of a plurality of desulfurization areas arranged at the upper part of the storage device 15 through a pump body 8, and the outlet valve of each desulfurization area is connected with the storage device 15. The pump body 8 is further connected to a pump body outlet valve 7, a first pump body inlet valve 9 and a second pump body inlet valve 10.
The number of the desulfurization zones is 2-7, and as an example, the number of the desulfurization zones is 4, namely a first desulfurization zone A, a second desulfurization zone B, a third desulfurization zone C and a fourth desulfurization zone D; the first desulfurization area A is provided with a first desulfurization area inlet valve 18 and a first desulfurization area outlet valve 19; the second desulfurization area B is provided with a second desulfurization area inlet valve 20 and a second desulfurization area outlet valve 21; a third desulfurization area inlet valve 22 and a third desulfurization area outlet valve 23 are arranged on the third desulfurization area C; the fourth desulfurization zone D is provided with a fourth desulfurization zone inlet valve 24 and a fourth desulfurization zone outlet valve 25.
In the working process, the lean solution input valve 4, the first pump body inlet valve 9, the pump body outlet valve 7, the first desulfurization area inlet valve 18 and the first desulfurization area outlet valve 19 are opened, the desulfurizer passes through the lean solution input valve 4 and the first pump body inlet valve 9 and enters the first desulfurization area A through the pump body outlet valve 7 and the first desulfurization area inlet valve 18 under the action of the pump body 8, when the desulfurizer in the first desulfurization area A reaches a preset liquid level, the desulfurizer automatically overflows into the storage device 15 through the first desulfurization area outlet valve 19, and the liquid level of the storage device 15 rises to indicate that the injection of the desulfurizer in the first desulfurization area A is completed. After the injection of the desulfurizer in the first desulfurization area A is completed, opening a second desulfurization area inlet valve 20 and a second desulfurization area outlet valve 21, closing a first desulfurization area inlet valve 18 and a first desulfurization area outlet valve 19 in sequence, enabling the desulfurizer to pass through a barren liquor input valve 4 and a first pump body inlet valve 9, entering a second desulfurization area B through a pump body outlet valve 7 and the second desulfurization area inlet valve 20 under the action of a pump body 8, and automatically overflowing into a storage device 15 through the second desulfurization area outlet valve 21 when the desulfurizer in the second desulfurization area B reaches a preset liquid level, wherein the liquid level of the storage device 15 rises to indicate that the injection of the desulfurizer in the second desulfurization area B is completed. And by analogy, conveying the desulfurizer to the third desulfurization zone C and the fourth desulfurization zone D, and after the injection of the desulfurizer is completed in the topmost fourth desulfurization zone D, continuing to operate the pump body 8 until the desulfurizer overflows into the storage device 15 through the fourth desulfurization zone D and reaches the preset liquid level of the storage device 15. The desulfurizing agents in the four desulfurization areas reach saturation after absorbing hydrogen sulfide, an inlet valve of the desulfurization areas can be opened, and the desulfurizing agents reversely flow under the action of gravity and are output through a rich liquid output valve 6. The desulfurizer in the storage 15 is saturated after absorbing hydrogen sulfide and can be directly output through the pump body 8, the pump body outlet valve 7 and the rich liquid output valve 6.
The storage device 15 is also connected with the bypass valve 5, and because the desulfurization agent amount in the storage device 15 is large, when the saturated desulfurization agent in the storage device 15 needs to be output, the bypass valve 5 can be opened, and the output of the desulfurization agent is accelerated. The storage 15 is further provided with a second liquid level meter 16 for monitoring the liquid level of the desulfurizing agent in the storage 15. In the utility model, after the discharged air is desulfurized by the storage device 15 and the plurality of desulfurization areas, the content of hydrogen sulfide in the discharged air is lower than 20mg/Nm3。
In the utility model, a partition plate 12 is arranged between the storage device 15 and the separator 1, between the storage device 15 and the desulfurization area, and between two adjacent desulfurization areas.
The gas distributor comprises an inverted U-shaped gas rising pipe 17, the bottom of the gas rising pipe 17 is inserted below the partition plate 12, and the top of the gas rising pipe 17 is communicated with the spray plate 11. Referring to fig. 2 and 3, the nozzle plate 11 includes a vertical main pipe 111 and a horizontal main pipe 112 which are communicated with each other, the top end of the vertical main pipe 111 is communicated with the top of the riser 17, the horizontal main pipe 112 is communicated with a plurality of branch pipes 113, and the branch pipes 113 are provided with a plurality of nozzle holes 114. The transverse main pipe 112 and the branch pipe 113 are both located below the liquid surface of the desulfurizing agent.
During the working process, the vent gas enters from the bottom of the riser 17, enters the vertical main pipe 111 after reaching the top of the riser 17, then enters each branch pipe 113 through the horizontal main pipe 112 downwards, is sprayed out from the spray holes 114, is in full contact with the desulfurizer, and has mass transfer and reaction, and the desulfurizer absorbs the hydrogen sulfide in the vent gas.
The utility model discloses in, orifice 114 evenly sets up on branch pipe 113, and orifice 114's aperture is 4 ~ 8mm, makes in the unloading can the homodisperse to the desulfurizer, increases the area of contact of unloading and desulfurizer, improves and absorbs desulfurization effect. As a preferable scheme, the spray holes 114 are positioned at the bottom of the branch pipe 113, namely the spray holes 114 are opened downwards, so that the dispersion effect of the vent gas in the desulfurizing agent can be promoted, and the absorption rate of the hydrogen sulfide can be improved.
As a preferred scheme, the top of the sulfur-containing gas emptying and desulfurizing device is provided with a defoaming wire mesh 32, the defoaming wire mesh is selected according to HG/T21618-.
The utility model discloses in, the outside of storage device 15 and each desulfurization district all is equipped with manhole 26 to satisfy the needs of inside maintenance, detection, maintenance.
The utility model provides a contain gas unloading desulphurization unit is skid-mounted structure, and the unloading is from the access device until discharging, all does not have valve class facility separation, and the flow of unloading is unobstructed, and whole device security is higher. The desulfurizer in the utility model is amine liquid or alcohol liquid. The storage amount of the desulfurizer in the storage device 15 is determined according to the emptying air amount of the temporary or emergency emptying of a specific crude oil station, and the amount of the desulfurizer stored in each desulfurization area is determined to meet the desulfurization requirement of emptying for 1-3 times.
The working principle of the utility model is as follows:
the desulfurizer respectively enters each desulfurization area under the action of the pump body 8 and then overflows from each desulfurization area into the storage device 15; the desulfurizing agent in the storage 15 can also be supplemented into each desulfurization zone through the pump body 8. The crude oil station sour vent first enters separator 1 from the bottom of the unit, where entrained droplets are removed in separator 1. The vent gas from which the liquid droplets are removed leaves the separator 1, enters the riser 17 in the storage device 15 upwards, enters the spray plate 11 in the storage device 15 and is sprayed out, and contacts with a desulfurizing agent in the storage device 15, and the desulfurizing agent performs primary absorption on hydrogen sulfide in the vent gas. Because the hydrogen sulfide is only absorbed once and can not reach the environmental protection index of the discharged air, the discharged air after primary absorption continuously enters the ascending pipe 17 in the first desulfurization area A upwards and then enters the spraying plate 11 in the first desulfurization area A and is sprayed out, and secondary absorption is carried out in the first desulfurization area A. And sequentially absorbing for three times and four times upwards until meeting the environmental protection index of discharged air, finally removing the desulfurizer liquid drops with the particle size of more than 100 mu m through a defoaming wire mesh 32, and discharging from an air outlet 28 at the top of the device.
The utility model provides a desulfurizer absorbs the hydrogen sulfide saturation back, can transport the desulfurizer that the oil field was concentrated and is built outward and handle regenerating unit, and after regenerating unit's processing, the desulfurizer can recycle. A sulfur recovery device can be arranged in a desulfurizer treatment and regeneration plant, so that the sulfur is reasonably utilized, and the pollution to the environment is reduced.
To sum up, the utility model is provided with a separator, a storage device and a plurality of desulfurization areas from bottom to top, the separator can remove liquid drops carried in the air, the storage device is used for containing the desulfurizer and pouring the desulfurizer into each desulfurization area arranged on the upper part of the storage device; gas distributors are arranged in the storage device and the desulfurization area; the gas distributor comprises an inverted U-shaped gas riser, the top of the gas riser is communicated with the vertical main pipe of the spray plate, the horizontal main pipe of the spray plate is communicated with a plurality of branch pipes, and the branch pipes are provided with a plurality of spray holes; the horizontal main pipe and the branch pipes are both positioned below the liquid level of the desulfurizer, the discharged air without liquid drops enters the gas distributor in the storage device, hydrogen sulfide is absorbed for the first time in the storage device, and then the discharged air continues to enter the gas distributors in the desulfurization areas upwards and then carries out sulfur treatmentHydrogen sulfide is absorbed for a plurality of times to ensure that the content of the hydrogen sulfide is lower than 20mg/Nm3. To sum up, the beneficial effects of the utility model are that: the hydrogen sulfide in the exhausted gas can be fully absorbed, the desulfurization effect of the exhausted gas is improved, and the quality of the surrounding environment of the oil field is improved; the whole device is of a skid-mounted structure, the manufacturing cost of equipment is low, the flow of the discharged air in the device is smooth and unobstructed, the safety is high, the desulfurizer is recycled, and the production cost is reduced.
Naturally, the present invention can be embodied in many other forms without departing from the spirit or essential attributes thereof, and it should be understood that various changes and modifications can be made by one skilled in the art without departing from the spirit or essential attributes thereof, and it is intended that all such changes and modifications be considered as within the scope of the appended claims.
Claims (9)
1. The device is characterized by comprising a separator, a storage device and a plurality of desulfurization areas, wherein the separator is used for removing liquid drops carried in the vent gas, the storage device is used for containing a desulfurizer, and the desulfurization areas are used for desulfurizing the vent gas; gas distributors are arranged in the storage device and the desulfurization area;
the storage device is respectively connected with a plurality of inlet valves of the desulfurization areas, and an outlet valve of each desulfurization area is connected with the storage device;
partition plates are arranged between the separator and the storage device, between the storage device and the desulfurization zone and between two adjacent desulfurization zones;
the gas distributor comprises an inverted U-shaped gas rising pipe, the bottom of the gas rising pipe is inserted below the partition plate, and the top of the gas rising pipe is communicated with the spray plate; the spray plate comprises a vertical main pipe and a transverse main pipe which are communicated with each other, the top end of the vertical main pipe is communicated with the top of the gas lift pipe, the transverse main pipe is communicated with a plurality of branch pipes, and the branch pipes are provided with a plurality of spray holes; the transverse main pipe and the branch pipes are both positioned below the liquid level of the desulfurizer.
2. The device for the vented desulfurization of sulfur-containing gas according to claim 1, wherein said separator is provided with an air inlet line and a blowdown line, and a plurality of liquid-blocking plates are provided inside said separator.
3. The apparatus for the vented desulfurization of sulfur-containing gas as claimed in claim 1, wherein said separator is externally provided with a first level meter for monitoring the level of the liquid in said separator in real time.
4. The sulfur-containing gas blowdown and desulfurization device of claim 2, wherein said liquid baffle has an angle of 10 to 45 degrees with the horizontal plane.
5. The apparatus for the vented desulfurization of sulfur-containing gas as claimed in claim 1, wherein said storage means is connected to a lean liquid input valve and a rich liquid output valve, and said storage means is further connected to a bypass valve.
6. The sulfur-containing gas vent desulfurization device as claimed in claim 1, wherein a second level meter is further provided on the storage device for monitoring the level of the desulfurizing agent in the storage device.
7. The device for the vented desulfurization of sulfur-containing gas as claimed in claim 1, wherein a manhole is provided outside both of said holder and said desulfurization zone.
8. The device for the vented desulfurization of sulfur-containing gas as claimed in claim 1, wherein said nozzle holes are located at the bottom of said branch pipes, and the diameter of said nozzle holes is 4-8 mm.
9. The device for the air-release desulfurization of sulfur-containing gas as claimed in claim 1, wherein the top of the device is provided with a defoaming wire mesh, and the defoaming wire mesh is provided with 15-35 layers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020953981.2U CN212819000U (en) | 2020-05-30 | 2020-05-30 | Contain sour gas unloading desulphurization unit |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020953981.2U CN212819000U (en) | 2020-05-30 | 2020-05-30 | Contain sour gas unloading desulphurization unit |
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| CN212819000U true CN212819000U (en) | 2021-03-30 |
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| CN202020953981.2U Active CN212819000U (en) | 2020-05-30 | 2020-05-30 | Contain sour gas unloading desulphurization unit |
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| CN (1) | CN212819000U (en) |
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