Recovery process of anion exchange resin in a solvent recovery process

A technology of exchange resin and anion, applied in the field of recovery process of ion exchange resin, can solve the problems of rising electrical conductivity, increasing production cost, blocking ion exchange channels, etc., to achieve the effect of improving exchange capacity, long service life and high safety performance.

Active Publication Date: 2019-05-21
BAODING SWAN NEW FIBER MFG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] 1. Ion exchange resin will be polluted or poisoned after long-term use;
[0006] 2. In the prior art, after long-term use of ion exchange resins, high-valent metal ions and various polymeric organic substances generate intolerant deposits and deposit inside the resin, blocking the channels of ion exchange and reducing the purification and recovery effect of the resin;
[0007] 3. As the ion exchange resin is used for a long time, the color of the resin will become darker and the volume will expand; the washing time will be prolonged, the conductivity will increase, and the regeneration operation will be difficult;
[0008] 4. The cost of replacing a new ion exchange resin is relatively high, which increases production costs

Method used

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  • Recovery process of anion exchange resin in a solvent recovery process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] Embodiment 1 Recovery process of anion exchange resin in a solvent recovery process

[0040] Anion exchange resin resuscitation fluid composition

[0041] Anion exchange resin resuscitating fluid of the present invention is alkaline common saline;

[0042] The alkaline salt solution is a solution formed by dissolving sodium chloride and sodium hydroxide in water;

[0043] The concentration of sodium chloride in the alkaline saline: 15%; the concentration of sodium hydroxide: 3%;

[0044] The amount of alkaline salt water: 58m 3 ;Specification of anion resin: 15m 3 .

[0045] Anion Exchange Resin Recovery Procedure

[0046] Anion exchange resin recovery was carried out three times; each recovery was divided into two steps of static and dynamic top water; after the third recovery was completed, positive washing and backwashing were performed, and regeneration was performed when the pH reached 9;

[0047] The regeneration volume is 3BV; 3BV refers to 3 times the volu...

Embodiment 2

[0068] Embodiment 2 Recovery process of anion exchange resin in a solvent recovery process

[0069] Anion exchange resin resuscitation fluid composition

[0070] Anion exchange resin resuscitating fluid of the present invention is alkaline common saline;

[0071] The alkaline salt solution is a solution formed by dissolving sodium chloride and sodium hydroxide in water;

[0072] The concentration of sodium chloride in the alkaline salt water: 13%; the concentration of sodium hydroxide: 2.5%;

[0073] The amount of alkaline salt water: 85m 3 ;Specification of anion resin: 15m 3 .

[0074] Anion Exchange Resin Recovery Procedure

[0075] Anion exchange resin recovery was carried out three times; each recovery was divided into two steps of static and dynamic top water; after the third recovery was completed, positive washing and backwashing were performed, and regeneration was performed when the pH reached 9;

[0076] The regeneration volume is 3BV; 3BV refers to 3 times th...

Embodiment 3

[0097] Example 3 Recovery process of anion exchange resin in a solvent recovery process

[0098] Anion exchange resin resuscitation fluid composition

[0099] Anion exchange resin resuscitating fluid of the present invention is alkaline common saline;

[0100] The alkaline salt solution is a solution formed by dissolving sodium chloride and sodium hydroxide in water;

[0101] The concentration of sodium chloride in the alkaline salt water: 15%; the concentration of sodium hydroxide: 2.5%;

[0102] The amount of alkaline salt water: 68m 3 ;Specification of anion resin: 15m 3 .

[0103] Anion Exchange Resin Recovery Procedure

[0104] Anion exchange resin recovery was carried out three times; each recovery was divided into two steps of static and dynamic top water; after the third recovery was completed, positive washing and backwashing were performed, and regeneration was performed when the pH reached 9;

[0105] The regeneration volume is 3BV; 3BV refers to 3 times the v...

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Abstract

The invention provides a resuscitation technology of an anion exchange resin during a solvent recovery process. The resuscitation technology comprises the resuscitation of the anion exchange resin. Anion exchange resin resuscitation fluid is adopted to be subjected to resuscitation on the anion exchange resin, wherein the concentration of sodium hydroxide in the resuscitation fluid is 2%-3%. The resuscitation technology is low in cost to use; change of anion exchange resin(15m<3>) costs about 380 thousand RMB per time, while recovery costs about 12 thousand RMB per time; the resuscitation technology has a high safety performance during the use procedure, does not damage the resin and the safety of workers during the operation process; meanwhile, the resuscitation technology does not need to change the original structures of the equipment, thereby having no harmful effects on anion-cation machine tool equipment.

Description

technical field [0001] The invention relates to a recovery process of an ion exchange resin, in particular to a recovery process of an anion exchange resin in a solvent recovery process. Background technique [0002] In the production of Lyocell fiber, the solvent (NMMO) needs to be purified and recovered. Anion and cation exchange resins are used for solvent purification. Anion and cation exchange resins will be polluted or poisoned after a long period of operation. Anion and cation exchange resins are mainly affected by the recovery of iron in solvents, etc. High-valent metal ions and various high-molecular organic substances generate intolerant deposits and deposit into the resin, blocking the ion exchange channel, thus affecting the normal ion exchange process of the resin. The specific performance is that the color of the resin becomes darker and the volume expands; Prolongation, difficulty in regeneration operation; increase in conductivity and other phenomena. [000...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J49/60B01J49/57
Inventor 赵志德高殿才杜树新蒋志君王文忠张红立曹刚
Owner BAODING SWAN NEW FIBER MFG CO LTD
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