CN220990032U - Water-gas separation and silencing device for tail gas of glacial acetic acid production process - Google Patents
Water-gas separation and silencing device for tail gas of glacial acetic acid production process Download PDFInfo
- Publication number
- CN220990032U CN220990032U CN202322570466.2U CN202322570466U CN220990032U CN 220990032 U CN220990032 U CN 220990032U CN 202322570466 U CN202322570466 U CN 202322570466U CN 220990032 U CN220990032 U CN 220990032U
- Authority
- CN
- China
- Prior art keywords
- tail gas
- water
- separation tank
- gas
- separation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000000926 separation method Methods 0.000 title claims abstract description 39
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 229960000583 acetic acid Drugs 0.000 title claims abstract description 14
- 239000012362 glacial acetic acid Substances 0.000 title claims abstract description 14
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 14
- 230000030279 gene silencing Effects 0.000 title claims abstract description 13
- 238000010521 absorption reaction Methods 0.000 claims abstract description 19
- 230000005587 bubbling Effects 0.000 claims abstract description 19
- 230000003584 silencer Effects 0.000 claims abstract description 12
- 230000001105 regulatory effect Effects 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 20
- 230000005484 gravity Effects 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 230000008030 elimination Effects 0.000 abstract description 2
- 238000003379 elimination reaction Methods 0.000 abstract description 2
- 230000000274 adsorptive effect Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses a water-gas separation and silencing device for tail gas of glacial acetic acid production process, which comprises a bubbling absorption tower and a separation tank, wherein the bubbling absorption tower is provided with a tail gas inlet, the separation tank is connected with an air inlet pipeline, the air inlet pipeline is connected to the top of the bubbling absorption tower, an exhaust automatic regulating valve is arranged in the air inlet pipeline, and a silencer is arranged in the connection of the exhaust pipeline of the separation tank. And the tail gas of the glacial acetic acid production process is discharged from the top of the bubbling absorption tower and enters the separation tank through the automatic gas discharge regulating valve, the water phase is separated from the tail gas under the action of partial centrifugal force and gravity, the water phase is discharged and recovered from the drain valve of the separation tank, and the tail gas enters the silencer from the top of the separation tank to reduce noise and is discharged. The separation tank is adopted to separate water from gas, so that water with acidity and corrosiveness can be separated from the tail gas; the tail gas no longer contains water; after entering the muffler, the tail gas is subjected to deceleration, noise elimination and noise reduction; thereby achieving the effects of water-gas separation and silencing.
Description
Technical Field
The utility model belongs to the technical field of water-gas separation and noise reduction, and particularly relates to a tail gas water-gas separation and noise reduction device.
Background
The existing glacial acetic acid production process tail gas treatment device is shown in fig. 1. The tail gas is discharged from the top of the bubbling absorption tower after being absorbed by the bubbling absorption tower, and is directly discharged into the atmosphere through an automatic regulating valve, and the tail gas discharged in the method is often entrained with water. This portion of the water tends to be acidic due to the nature of the bubble column and is corrosive. When the acidic water in the exhaust falls into a building or equipment, the building or equipment is corroded, resulting in damage. Burn and other conditions can be caused when the water is sprayed to a person. Therefore, the method has potential safety hazard and can cause environmental pollution. And the exhaust can be discharged with high noise, and noise pollution can be caused.
Disclosure of utility model
The utility model aims to provide a water-gas separation and silencing device for tail gas of glacial acetic acid production process, which aims to solve the problems of high water entrainment and noise in devices in the prior art.
The tail gas water-gas separation and silencing device for the glacial acetic acid production process is characterized by comprising a bubbling absorption tower and a separation tank, wherein the bubbling absorption tower is provided with a tail gas inlet, the separation tank is connected with an air inlet pipeline, the air inlet pipeline is connected to the top of the bubbling absorption tower, an exhaust automatic regulating valve is arranged in the air inlet pipeline, and a silencer is arranged in the connection of the exhaust pipeline of the separation tank.
A drain valve is arranged at the bottom of the separating tank.
The silencer comprises a cylinder body, wherein two ends of the cylinder body are respectively provided with an air inlet and an air outlet, an inner cylinder is arranged in the cylinder body and communicated with the air inlet into a whole, and the cylinder wall is provided with air holes.
The air outlet of the silencer is communicated with the environment.
The separating tank is internally provided with a circular body, and the tail gas enters the separating tank from a circular tangent angle to form the spiral motion of the tail gas.
The inner cylinder is filled with adsorptive substances.
And the tail gas of the glacial acetic acid production process is discharged from the top of the bubbling absorption tower and enters the separation tank through the automatic gas discharge regulating valve, the water phase is separated from the tail gas under the action of partial centrifugal force and gravity, the water phase is discharged and recovered from the drain valve of the separation tank, and the tail gas enters the silencer from the top of the separation tank to reduce noise and is discharged.
The tail gas entering the silencer firstly enters the inner cylinder and then is noise-reduced through adsorptive substances, and is discharged to the outer cylinder through the air holes on the wall of the inner cylinder and is discharged from the outer cylinder.
The tail gas enters the separating tank from a circular tangential angle, so that the tail gas entering the separating tank moves spirally, thereby generating centrifugal force and separating water and gas more effectively.
The utility model relates to a tail gas water-gas separation and silencing device, which is characterized in that a separation tank is adopted to separate water from gas, so that acidic and corrosive water can be separated from the gas; the tail gas no longer contains water; after entering the muffler, the tail gas is subjected to deceleration, noise elimination and noise reduction; thereby achieving the effects of water-gas separation and silencing.
Drawings
Fig. 1 is a diagram of a conventional exhaust gas treatment device.
Fig. 2 is a schematic structural diagram of an exhaust gas treatment device according to an embodiment of the present utility model.
Fig. 3 is a schematic view of a muffler according to an embodiment of the present utility model.
Fig. 4 is a schematic plan view of a separator.
Reference numerals in the drawings: 1. the device comprises a position bubbling absorption tower, a separation tank, a water discharge valve, a muffler, an exhaust automatic regulating valve and a muffler, wherein the separation tank is arranged in the position bubbling absorption tower; 6. a cylinder; 7. an air inlet; 8. an air outlet; 9. an inner cylinder; 10. has a circular shape.
Detailed Description
The utility model provides a glacial acetic acid production technology tail gas water vapor separation and silencing device, is including bubbling absorption tower 1, separator tank 2, and bubbling absorption tower 1 is equipped with the tail gas import, and separator tank 2 is connected with the admission line, and the admission line is connected to bubbling absorption tower 1 top, installs exhaust automatic regulating valve 5 in the admission line, and muffler 4 is installed in the exhaust line connection of separator tank 2. A drain valve 3 is installed at the bottom of the separation tank 2. The silencer 4 comprises a cylinder 6, an air inlet 7 and an air outlet 8 are respectively arranged at two ends of the cylinder 6, an inner cylinder 9 is arranged in the cylinder 6 and communicated with the air inlet 7 into a whole, and air holes are formed in the wall of the inner cylinder 9. The inner tube 9 is filled with an adsorptive substance.
The tail gas of the glacial acetic acid production process is discharged from the top of the bubbling absorption tower 1, enters the separation tank 2 through the automatic exhaust regulating valve 5, is separated from the tail gas under the action of partial centrifugal force and gravity of the water phase, is discharged and recovered from the drain valve 3 at the bottom of the separation tank 2, and enters the silencer 4 from the top of the separation tank 2 to reduce noise and is discharged. The separator tank 2 has a circular body 10.
The tail gas entering the muffler 4 firstly enters the inner cylinder and then is noise-reduced through adsorptive substances, and is discharged to the outer cylinder through the air holes on the wall of the inner cylinder and is discharged from the outer cylinder.
The tail gas enters the separating tank through the tangential angle of the circular body 10, so that the tail gas entering the separating tank can spirally move, thereby generating centrifugal force and enabling water and gas to be separated more effectively.
Claims (4)
1. The tail gas water-gas separation and silencing device for the glacial acetic acid production process is characterized by comprising a bubbling absorption tower and a separation tank, wherein the bubbling absorption tower is provided with a tail gas inlet, the separation tank is connected with an air inlet pipeline, the air inlet pipeline is connected to the top of the bubbling absorption tower, an exhaust automatic regulating valve is arranged in the air inlet pipeline, and a silencer is arranged in the connection of the exhaust pipeline of the separation tank.
2. The tail gas water-gas separation and silencing device for glacial acetic acid production process according to claim 1, wherein a drain valve is arranged at the bottom of the separation tank.
3. The tail gas water-gas separation and silencing device for glacial acetic acid production process according to claim 1, wherein the silencer comprises a cylinder body, two ends of the cylinder body are respectively provided with an air inlet and an air outlet, an inner cylinder is arranged in the cylinder body and communicated with the air inlet into a whole, and air holes are formed in the wall of the inner cylinder.
4. The tail gas water-gas separation and silencing device for glacial acetic acid production process according to claim 1, wherein the air outlet of the silencer is open to the environment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202322570466.2U CN220990032U (en) | 2023-09-21 | 2023-09-21 | Water-gas separation and silencing device for tail gas of glacial acetic acid production process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202322570466.2U CN220990032U (en) | 2023-09-21 | 2023-09-21 | Water-gas separation and silencing device for tail gas of glacial acetic acid production process |
Publications (1)
Publication Number | Publication Date |
---|---|
CN220990032U true CN220990032U (en) | 2024-05-24 |
Family
ID=91114633
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202322570466.2U Active CN220990032U (en) | 2023-09-21 | 2023-09-21 | Water-gas separation and silencing device for tail gas of glacial acetic acid production process |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN220990032U (en) |
-
2023
- 2023-09-21 CN CN202322570466.2U patent/CN220990032U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN220990032U (en) | Water-gas separation and silencing device for tail gas of glacial acetic acid production process | |
CN105964081A (en) | Small-sized multilayer dust removal and desulfurization device | |
CN206996240U (en) | A kind of vortex pulse type reactor | |
CN105749710A (en) | Marine exhaust gas SOx removal device for rotary spraying refluxing bubble tower | |
CN207085657U (en) | A kind of desulfurizing tower | |
CN206444440U (en) | Modified desulfurizing tower | |
CN204865511U (en) | A desulfurization dust remover for brickfield | |
CN212492213U (en) | Gas purification system | |
CN204563780U (en) | Barb demister optimized by a kind of streamlined two passage bands | |
CN202289832U (en) | Gas-liquid centrifugal separation structure at low flow rate | |
CN207813698U (en) | Tail gas smoke abatement device of offshore wind power self-elevating mounting platform generator set | |
CN107588319B (en) | Energy-saving environment-friendly vibration reduction air storage tank | |
CN208448942U (en) | A kind of hydrochloric acid entrucking exhaust gas processing device | |
CN205435388U (en) | Small -size clean cigarette equipment | |
CN111036401A (en) | Wet electrostatic filter bag dust collector | |
CN210645843U (en) | Waste gas desulfurization equipment | |
CN204246865U (en) | A kind of water vapor separation system | |
CN217329003U (en) | Steam condensate buffer tank | |
CN201271562Y (en) | High-efficient wet-type desulfurizer | |
CN221230296U (en) | Ammonia gas collecting device in urea dissolving area of power plant | |
CN219252210U (en) | Efficient desulfurization sleeve pipe rotary flat desulfurization tower device | |
CN202137061U (en) | Terminal catcher of residual formaldehyde in tail gas | |
CN212855261U (en) | Waste gas treatment device | |
CN209464822U (en) | Small-sized emission-control equipment | |
CN212881768U (en) | Waste gas absorption tower |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |