Gas-liquid separation device for cresol production
By designing a gas-liquid separation device for cresol production, the cresol solution is separated by centrifugal force and adsorption of the adsorption net and drive components, and ensuring sealing through anti-aircraft structure, gas overflow during cresol production is solved The problem of waste of raw materials has achieved efficient and environmentally friendly separation.
Patent Information
- Application Number
- CN202421245272.3
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-06-03
- Publication Date
- 2025-02-14
- Estimated Expiration
- 2034-06-03
AI Technical Summary
During the cresol production process, the gas contains atomized cresol solution and sulfur dioxide gas overflow, resulting in environmental pollution and equipment corrosion, and at the same time, there are problems of waste of raw materials and high production costs.
Design a gas-liquid separation device for producing cresol, including a separation tank, air inlet, air outlet, drain port and drain pipe, and use an adsorption net and drive assembly to separate the cresol solution in the gas through centrifugal force and adsorption, and Sealability is ensured through an anti-aircraft structure.
The rapid and effective separation of cresol solution in the gas is achieved, which reduces raw material waste and production costs, while avoiding the leakage of harmful gases, and improving the environmental protection and safety of the device.
Smart Images

Figure CN222468498U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of cresol production equipment, in particular to a cresol production gas-liquid separation device. Background Art
[0002] In the production process of cresol, when the sodium cresol alkali fusible solution produced by the alkali fusion process undergoes an acidification process and undergoes an acidification reaction to generate acidic cresol, phenolic gas and residual sulfur dioxide gas used for acidification will overflow through the venting phase of various equipment and storage tanks and emanate into the atmosphere, with a strong odor, causing pollution to the surrounding environment and affecting the lives of surrounding residents. At the same time, sulfur dioxide gas also causes corrosion to the equipment and pipelines in the production workshop, greatly affecting the service life of the equipment and pipelines. At the same time, since the gas generated by the sodium cresol alkali fusible solution in the acidification process contains an atomized solution, it contains part of the cresol solution. If it is not collected and recycled, it will cause a waste of production raw materials and increase production costs. During the existing gas-liquid separation, due to the low proportion of the atomized solution in the gas, the position of the drain port remains open, so part of the gas will overflow, causing environmental pollution. At the same time, the atomized solution is difficult to be more thoroughly adsorbed and settled inside the separation device. Utility Model Content
[0003] In view of the above situation, in order to overcome the defects of the prior art, the purpose of the utility model is to provide a cresol production gas-liquid separation device, which can quickly and effectively separate the cresol solution in the gas, reduce the waste of raw materials, reduce production costs, and no harmful gases will leak during the separation process, thus having good environmental protection.
[0004] To achieve the above-mentioned purpose, the utility model provides the following technical scheme: a gas-liquid separation device for cresol production, comprising a separation tank, the separation tank being provided with an air inlet and an air outlet, a liquid discharge port being provided at the bottom of the separation tank, the air inlet being arranged along the tangent direction of the separation tank, and also comprising a liquid discharge pipe connected to the liquid discharge port, and the liquid discharge pipe being provided with an anti-overgas structure, and also comprising a collecting component, the collecting component comprising an adsorption net located inside the separation tank, and the adsorption net being located between the air inlet and the air outlet, and also comprising a driving component for driving the adsorption net to rotate, and the air outlet being located on a side of the separation tank away from the air inlet.
[0005] After the gas to be treated is introduced into the air inlet pipe through the air pump, the high-speed air flow will rotate at high speed inside the separation tank, and the atomized cresol solution in the gas will be separated to the inner wall of the separation tank by centrifugal force. When the gas passes through the adsorption net, the solution contained in the gas will be adsorbed again under the action of the adsorption net to achieve a higher separation effect of the gas containing the atomized solution. The gas that has passed the adsorption net will be discharged through the outlet, and the gas after discharge will be centrally treated.
[0006] As a preferred technical solution of the utility model, the anti-overgassing structure is a U-shaped air blocking tube, and the air blocking tube is connected to the drainage tube.
[0007] When the separated solution is less, the solution will stay in the choke tube part, thereby preventing the gas from overflowing from the drain port.
[0008] As a preferred technical solution of the utility model, the adsorption net is made of polymer resin material.
[0009] As a preferred technical solution of the utility model, it also includes an exhaust pipe connected to the gas outlet, and the exhaust pipe is coaxially arranged with the separation tank.
[0010] As a preferred technical solution of the utility model, the driving assembly includes a main shaft rotatably installed inside the separation tank and a first rotating shaft arranged perpendicular to the axis of the main shaft, the adsorption net is fixedly installed on the main shaft and a driving bevel gear is installed on the main shaft, and a driven bevel gear meshing with the driving bevel gear is installed on the first rotating shaft.
[0011] The meshing of the active bevel gear and the driven bevel gear drives the adsorption net to rotate rapidly, and the solution adsorbed on the adsorption net is thrown off by centrifugal force.
[0012] As a preferred technical solution of the utility model, it also includes an intake pipe connected to the air inlet, a second rotating shaft is rotatably installed inside the intake pipe, and a turbine is installed on one side of the second rotating shaft located inside the intake pipe, and the second rotating shaft extends out of the intake pipe and is connected to the first rotating shaft through a gear belt.
[0013] By arranging a turbine inside the intake pipe, the high-speed airflow will drive the turbine to rotate, thereby driving the second rotating shaft to rotate, and the first rotating shaft and the second rotating shaft connected by the belt will rotate synchronously.
[0014] Compared with the prior art, the beneficial effects of the utility model are:
[0015] It can separate the cresol solution contained in the gas after the acidification reaction, and ensure the sealing of the device during the separation process to avoid the leakage of harmful gases, thereby improving the practical safety and environmental protection of the equipment.
[0016] Reduce the cost of device manufacturing and practicality, while improving the efficiency of solution separation. BRIEF DESCRIPTION OF THE DRAWINGS
[0017] Figure 1 It is a schematic structural diagram of the overall shaft side of the utility model.
[0018] Figure 2 It is a structural schematic diagram of the overall internal front of the utility model.
[0019] Figure 3 It is a schematic diagram of the overall internal axonometric structure of the utility model.
[0020] Figure 4 It is a schematic diagram of the structure of the internal axial side of the intake pipe of the utility model. DETAILED DESCRIPTION
[0021] The following will be combined with the drawings in the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.
[0022] See also Figure 1-4 , a gas-liquid separation device for cresol production, comprising a separation tank 1, wherein the separation tank 1 is provided with an air inlet and an air outlet, and the bottom of the separation tank 1 is provided with a liquid discharge port, and when in use, it also comprises an exhaust pipe 6 connected with the air outlet, and also comprises an air inlet pipe 2 connected with the air inlet, wherein the air inlet is arranged along the tangential direction of the separation tank 1, and through the air inlet pipe 2 arranged along the tangential direction of the separation tank 1, when the gas to be treated is passed into the air inlet pipe 2 through the air pump, the high-speed flowing airflow will rotate at a high speed inside the separation tank 1, and the atomized cresol solution in the gas is separated onto the inner wall of the separation tank 1 by centrifugal force, so that the separation effect is good and the structure is practical, the air outlet is located on the side of the separation tank 1 away from the air inlet, and the gas separated by centrifugation will move toward the air outlet, and also comprises a collecting component, wherein the collecting component comprises an adsorption net 8 located inside the separation tank 1, and the adsorption net 8 is located between the air inlet and the air outlet, When the gas passes through the adsorption net 8, the solution contained in the gas will be adsorbed again under the action of the adsorption net 8 to achieve a higher gas-atomized solution separation effect. The gas passing through the adsorption net 8 will be discharged through the gas outlet. The gas after discharge is centrally processed. The exhaust pipe 6 is coaxially arranged with the separation tank 1. The position of the exhaust pipe 6 is located at the center of the separation tank 1, which prevents the separated solution from easily entering the exhaust pipe 6. The separated solution will gather at the bottom of the separation tank 1 and be discharged through the liquid discharge port. The liquid discharge pipe 4 also includes a liquid discharge pipe 4 connected to the liquid discharge port, and the liquid discharge pipe 4 is provided with an anti-gassing structure. The anti-gassing structure is a U-shaped gas blocking pipe 5, and the gas blocking pipe 5 is connected to the liquid discharge pipe 4. By setting the U-shaped gas blocking pipe 5, when the separated solution is less, the solution will stay in the gas blocking pipe 5 part, thereby preventing the gas from overflowing from the liquid discharge port and ensuring the sealing of the device.
[0023] Other specific practicable schemes of the utility model, as can be seen from the attached drawings, also include a driving component for driving the adsorption net 8 to rotate, the adsorption net 8 is made of a polymer resin material, the polymer resin can efficiently adsorb the cresol solution in the gas, and the mesh of the adsorption net 8 is honeycomb-shaped to increase the contact area with the gas, thereby improving the adsorption effect, the driving component includes a main shaft 9 rotatably installed inside the separation tank 1 and a first rotating shaft 7 perpendicular to the axis of the main shaft 9, the adsorption net 8 is fixedly installed on the main shaft 9 and a driving bevel gear 10 is installed on the main shaft 9, and a driven bevel gear 11 meshing with the driving bevel gear 10 is installed on the first rotating shaft 7. When in use, a driving motor can be installed on the separation tank 1, and the first rotating shaft 7 is driven to rotate by the driving motor, and the adsorption is driven under the meshing of the driving bevel gear 10 and the driven bevel gear 11. The rapid rotation of the attached net 8 not only increases the contact effect with the gas during the rotation of the adsorption net 8, but also can throw off the solution adsorbed on the adsorption net 8 through centrifugal force, further improving the separation effect while ensuring that the adsorption net 8 can continue to effectively adsorb. The second rotating shaft 3 is rotatably installed inside the intake pipe 2, and a turbine 12 is installed on one side of the second rotating shaft 3 located inside the intake pipe 2. The side of the second rotating shaft 3 extending out of the intake pipe 2 is connected to the first rotating shaft 7 through a gear belt. In order to further reduce the manufacturing cost of the device, a turbine 12 is arranged inside the intake pipe 2, and the high-speed airflow will drive the turbine 12 to rotate, thereby driving the second rotating shaft 3 to rotate, and the first rotating shaft 7 and the second rotating shaft 3 connected by the belt will rotate synchronously. The use of this mechanism can greatly reduce the production cost and practical cost of the device.
[0024] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.
Claims
1. A gas-liquid separation device for cresol production, comprising a separation tank (1), wherein the separation tank (1) is provided with an air inlet and an air outlet, and the bottom of the separation tank (1) is provided with a liquid discharge port, characterized in that ; The air inlet is arranged along the tangent direction of the separation tank (1); It also includes a liquid discharge pipe (4) connected to the liquid discharge port, and the liquid discharge pipe (4) is provided with an anti-gassing structure; It also includes a collecting assembly, wherein the collecting assembly includes an adsorption net (8) located inside the separation tank (1), and the adsorption net (8) is located between the air inlet and the air outlet; It also includes a driving assembly for driving the adsorption net (8) to rotate; The gas outlet is located on a side of the separation tank (1) away from the gas inlet.
2. A gas-liquid separation device for cresol production according to claim 1, characterized in that: The anti-overgassing structure is a U-shaped air blocking tube (5), and the air blocking tube (5) is connected to the liquid discharge tube (4).
3. A gas-liquid separation device for cresol production according to claim 1, characterized in that: The adsorption net (8) is made of polymer resin material.
4. A gas-liquid separation device for cresol production according to claim 1, characterized in that: It also comprises an exhaust pipe (6) connected to the gas outlet, wherein the exhaust pipe (6) is arranged coaxially with the separation tank (1).
5. A gas-liquid separation device for cresol production according to claim 1, characterized in that: The driving assembly comprises a main shaft (9) rotatably mounted inside the separation tank (1) and a first rotating shaft (7) arranged perpendicular to the axis of the main shaft (9); the adsorption net (8) is fixedly mounted on the main shaft (9) and a driving bevel gear (10) is mounted on the main shaft (9); and a driven bevel gear (11) meshing with the driving bevel gear (10) is mounted on the first rotating shaft (7).
6. A gas-liquid separation device for cresol production according to claim 5, characterized in that: It also includes an intake pipe (2) connected to the air inlet, a second rotating shaft (3) is rotatably mounted inside the intake pipe (2), a turbine (12) is mounted on one side of the second rotating shaft (3) located inside the intake pipe (2), and the side of the second rotating shaft (3) extending out of the intake pipe (2) is connected to the first rotating shaft (7) via a gear belt.