Monomer-containing solvent refining system and process

A solvent refining and monomer technology, applied in sustainable manufacturing/processing, chemical industry, carboxylate preparation, etc., can solve the problem of low mass transfer and heat transfer efficiency, high content of polymerization inhibitor, and uneven distribution of gas-liquid two-phase To achieve the effect of strengthening gas-liquid mass transfer and heat transfer, reducing the degree of wall flow, and enhancing the separation effect

Active Publication Date: 2022-08-05
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] (1) The polymerization inhibitor has the risk of entraining the liquid foam to the top of the tower to recover the solvent, resulting in a high content of the polymerization inhibitor in the recovered solvent, which will affect the reaction time and rate of the free radical polymerization of the monomer after the solvent is reused;
[0004] (2) The reaction product of organic base and monomer still has the risk of self-polymerization in the tower kettle and the risk of organic base self-decomposition, and the selection of organic base requires long-term operation to verify its feasibility;
[0006] (1) Compared with the plate tower, the packed tower has higher separation efficiency under reduced pressure and normal pressure operation, but the packing cannot be directly used for materials that are easy to polymerize, and its anti-blocking performance is not as good as the plate tower;
[0007] (2) The void ratio between the packing and the tower wall in the packed tower is higher than that inside the packing, so when the liquid flows down the packing layer, it tends to gradually concentrate on the tower wall, so that the liquid flow near the tower wall gradually increases (ie Wall flow effect) will make the gas-liquid two-phase distribution in the packing layer uneven, thereby reducing the mass transfer and heat transfer efficiency

Method used

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  • Monomer-containing solvent refining system and process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] A monomer-containing solvent refining system, comprising a crude solvent tank 1, a weight-removing tower 6, a flash tank 10, and a reboiler 5; the crude solvent tank 1 outlet pipeline is connected to the weight-removing tower 6 stills, the weight-removing tower 6 stills And each section in the tower is connected to the flash tank 10 through the overflow pipeline, and a branch after the liquid phase outlet pipeline of the flash tank 10 and the outlet pipeline at the bottom of the weight-removing tower 6 is brought together is connected with the reboiler 5, and the other is connected to the reboiler 5. The branch is connected with the waste liquid tank 4; the outlet pipeline of the reboiler 5 goes to the weight-removing tower 6; Condenser 7 is connected; the liquid phase outlet pipeline of weight-removing tower condenser 7 and the liquid-phase outlet pipeline of weight-removing tower 6 tower top are brought together and are connected with recovery solvent tank 15, and the ...

Embodiment 2

[0047] The monomer-containing solvent refining system used in this example is based on the system in Example 1, and a corrugated buckle tube is added between the packing and the wall of the weight-removing tower. The outer diameter of the buckle tube is 40mm, and the buckle tube is The center distance is 80mm. In addition, the discharge pipe of the reboiler 5 is divided, and one branch pipe goes to the 6 tower stills of the weight-removing tower, and the other branch pipe goes to the buckle pipe in the packing, and the outlet end pipeline of the buckle pipe is in phase with the 6 tower stills of the weight-removing tower. connect.

[0048] A monomer-containing solvent refining process, comprising the following processes:

[0049] The crude solvent from the crude solvent tank 1 is sent to the weight-removing tower 6 with a flow of 5000kg / h, and the light component at the top of the tower is condensed by the weight-removing tower condenser 7 and enters the recovery solvent tank...

Embodiment 3

[0052] The monomer-containing solvent refining system used in this example is based on the system in Example 2, and a corrugated buckle tube of the same specification is added at the position directly opposite to the corrugated buckle tube; in addition, the outlet of the reboiler 5 A branch is added to the material pipe, which leads to the additional buckle pipe, and the outlet end pipeline of the buckle pipe is also connected to the 6 column kettle of the weight-removing tower.

[0053] A monomer-containing solvent refining process, comprising the following processes:

[0054] The crude solvent from the crude solvent tank 1 is sent to the weight-removing tower 6 with the flow rate of the tower design feed load upper limit 10000kg / h, and the light component at the top of the tower is condensed by the weight-removing tower condenser 7 with a flow rate of 9848kg / h Enter the recovery solvent tank 15 . A part of the heavy components of the tower kettle is transported to the waste...

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Abstract

The invention discloses a monomer-containing solvent refining system and process. The system comprises a crude solvent tank and a heavy component removal tower, an outlet pipeline of the crude solvent tank is connected with a de-heavy tower kettle, the tower kettle and all sections in the tower are connected to a flash tank through overflow pipelines, a branch formed by converging a liquid phase outlet pipeline of the flash tank and an outlet pipeline at the bottom of the tower is connected with a reboiler, and the other branch is connected with a waste liquid tank; an outlet pipeline of the reboiler is communicated with the de-heavy tower; a gas phase outlet pipeline at the top of the tower and a gas phase outlet pipeline of the flash tank are converged and then connected with a condenser of the de-heavy tower; and a liquid phase outlet pipeline of the heavy component removal tower condenser and a liquid phase outlet pipeline at the tower top are converged and then are connected with a solvent recovery tank. According to the invention, the solvent containing the easily polymerizable monomer is refined, and the organic solvent can be obtained through high-efficiency and high-purity purification without adding a polymerization inhibitor or organic alkali.

Description

technical field [0001] The invention relates to a system and a process, in particular to a monomer-containing solvent refining system and process, belonging to the technical field of solvent refining. Background technique [0002] The polyacrylic acid thickener is made of acrylic acid as the main raw material, and the self-polymerization and crosslinking of the acrylic monomer are realized by the crosslinking agent under the action of the initiator, and then the polyacrylic acid thickening agent with super large molecular weight is obtained. The solvents used in the reaction are ethyl acetate and cyclohexane, the monomer conversion rate is 99%, the reaction product is a solid material, and the crude solvent needs to be purified and reused after the solid product is filtered. Among them, the impurities in the filtrate are mainly acrylic acid, ethyl propionate and oligomers of acrylic acid, but the content of acrylic acid and its oligomers in the solvent is higher than 300ppm ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C69/14C07C67/54C07C13/18C07C7/04B01D3/42B01D3/32B01D3/14
CPCC07C67/54C07C7/04B01D3/148B01D3/32B01D3/42B01D3/4205C07C2601/14C07C69/14C07C13/18Y02P20/10
Inventor 彭冬冬肖铭王峤李兴伟曾雄伟郭燕妮王瑾胡展乔小飞
Owner WANHUA CHEM GRP CO LTD
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