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Molecular sieve deiodination agent preparation method and molecular sieve deiodination agent

A molecular sieve and deiodination technology, applied in the chemical industry, can solve the problems of poor removal effect, adverse effects of subsequent application of acetic acid, and high iodide removal cost, and achieve the effects of reducing production and processing costs, low prices, and reduced usage.

Pending Publication Date: 2020-02-04
JIANGSU SOPO CHEM +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Based on this, it is necessary to provide a preparation method of a molecular sieve deiodination agent and a molecular sieve deiodination agent for the current problems that the removal cost of iodide in acetic acid is relatively high, and the removal effect is poor, and it is easy to bring adverse effects on the subsequent application of acetic acid.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] The molded mordenite molecular sieve is loaded on the ion exchange column; the metal salt Cu(NO 3 ) 2Dissolve in deionized water to form a salt solution containing non-silver metal ions; put the salt solution containing non-silver metal ions at a temperature of 60°C at a liquid hourly space velocity LHSV for 4h -1 The speed continues to pass through the ion exchange column equipped with mordenite molecular sieve, and the flow time is controlled at 20-30h, and the non-silver metal ions are exchanged with the cations in the mordenite molecular sieve; the molecular sieve is washed with deionized water, and the non-silver metal ion is removed The ionized mordenite molecular sieve is dried in an oven at a temperature of 120 DEG C to obtain a molecular sieve deiodination agent containing non-silver metal copper ions.

[0031] Ion exchange column refers to a columnar pressure vessel used for ion exchange reaction, and it is an exchange device for column method ion exchange. ...

Embodiment 2

[0034] Install the molecular sieve on the ion exchange column; put the metal salt Zn(NO 3 ) 2 Dissolve in deionized water to form a salt solution containing non-silver metal ions; set the salt solution containing non-silver metal ions at a temperature of 80°C at a liquid hourly space velocity LHSV for 3h -1 The speed continues to pass through the ion exchange column equipped with molecular sieves, and the flow time is controlled at 20-30h, so that the molecular sieves are loaded with non-silver metal ions; the molecular sieves are washed with deionized water, and the molecular sieves that have been loaded with non-silver metal ions are taken out. drying in an oven at 120°C to obtain a molecular sieve deiodination agent containing non-silver metal zinc ions.

Embodiment 3

[0036] Install the molecular sieve on the ion exchange column; put the metal salt Hg(NO 3 ) 2 Dissolve in deionized water to form a salt solution containing non-silver metal ions; put the salt solution containing non-silver metal ions at a temperature of 100°C at a liquid hourly space velocity LHSV for 4h -1 The speed continues to pass through the ion exchange column equipped with molecular sieves, and the flow time is controlled at 20-30h, so that the molecular sieves are loaded with non-silver metal ions; the molecular sieves are washed with deionized water, and the molecular sieves that have been loaded with non-silver metal ions are taken out. drying in an oven at 120°C to obtain a molecular sieve deiodination agent containing non-silver metal mercury ions.

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Abstract

The invention relates to a molecular sieve deiodination agent preparation method and a molecular sieve deiodination agent. The method comprises: loading a molecular sieve on an ion exchange column; dissolving a non-silver metal salt in deionized water to form a salt solution containing non-silver metal ions; making the salt solution containing the non-silver metal ions continuously pass through the ion exchange column filled with the molecular sieve at a temperature of 60-100 DEG C, wherein the passing time is controlled at 20-30 h, so that the non-silver metal ions are loaded in the molecularsieve; and washing the molecular sieve with deionized water, taking out the molecular sieve loading the non-silver metal ions, and drying to obtain the molecular sieve deiodination agent containing the non-silver metal ions. According to the invention, the molecular sieve deiodination agent is low in cost, and can react with the organic iodine or inorganic iodine in acetic acid to generate iodideprecipitate, so that the iodine content in acetic acid can be reduced by 50-95%; and by combining the molecular sieve deiodination agent and the existing silver-loading ion exchange resin or silver-loading molecular sieve, the use amount of the silver-containing deiodination agent can be greatly reduced, so that the iodine element in acetic acid can meet the specified requirements, and the adverse effects on the subsequent industrial production taking the acetic acid as the raw material are avoided.

Description

technical field [0001] The invention relates to the technical field of chemical industry, in particular to a preparation method of a molecular sieve deiodination agent and the molecular sieve deiodination agent. Background technique [0002] As an important chemical basic raw material, acetic acid has a very wide range of uses. Industrial acetic acid is mainly obtained from methanol through low-pressure carbonylation. Since iodide is used as an auxiliary agent for metal catalysts in this process, there is a certain amount of iodide and its derivatives in the final product. Although most of the iodide can be removed by traditional distillation and rectification, it requires a lot of heat and increases the cost, and a small amount of iodide will still remain in acetic acid. The presence of these iodides has a greater impact on the subsequent application of acetic acid, especially the production process of iodine-sensitive metal catalysts. For example: an important use of ace...

Claims

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Application Information

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IPC IPC(8): B01J20/18B01J20/30B01J20/32B01D15/08
CPCB01J20/186B01J20/3092B01J20/3236B01D15/08
Inventor 朱桂生周爱华赵禄强邵守言谢萍朱杰王忠华陈钢
Owner JIANGSU SOPO CHEM
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