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Composite low solid mercury catalyst used for acetylene hydrochlorination and preparation method thereof

A mercury catalyst and mercuric chloride technology, which is applied in the direction of physical/chemical process catalysts, hydrogen halide addition preparation, chemical instruments and methods, etc., can solve the problems of low catalyst stability, high cost, poor activity, etc., and achieve improved activity and stability, low price, and the effect of reducing volatilization

Active Publication Date: 2015-11-25
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In order to overcome the shortcomings of large pollution, high cost, low catalyst stability and poor activity in the existing preparation methods of low-mercury catalysts, the invention provides a preparation method of a composite low-mercury catalyst for acetylene hydrochlorination

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] 1. The activated carbon is pretreated to remove the ash, and dried to constant weight at 120°C to obtain the pretreated activated carbon;

[0033] 2. Prepare a 10wt% hydrochloric acid aqueous solution with a volume of 2.5L, dissolve 70g of mercuric chloride and 10g of potassium chloride in the hydrochloric acid aqueous solution, and use it as impregnation solution A;

[0034] 3. Weigh 1 kg of pretreated activated carbon dried to constant weight and add it to impregnating solution A, soak for 15 hours at 20°C, take out the activated carbon carrier impregnated with active components, and dry at 120°C to constant weight;

[0035] 4. Prepare a 10wt% hydrochloric acid aqueous solution with a volume of 2.5L, dissolve 30g copper chloride and 10g cerium chloride in the hydrochloric acid aqueous solution, and use it as the impregnation solution B;

[0036] 5. Add the impregnated activated carbon obtained in step 3 into the impregnation solution B, impregnate at 25°C for 15 hours...

Embodiment 2

[0039] 1. The activated carbon is pretreated to remove the ash, and dried to constant weight at 120°C to obtain the pretreated activated carbon;

[0040] 2. Prepare a 5wt% hydrochloric acid aqueous solution with a volume of 2.5L, dissolve 80g of mercuric chloride and 100g of potassium chloride in the hydrochloric acid aqueous solution, and use it as impregnation solution A;

[0041] 3. Weigh 1 kg of pretreated activated carbon dried to constant weight and add it to impregnating solution A, soak at 80°C for 15 hours, take out the activated carbon carrier impregnated with active components, and dry at 120°C to constant weight;

[0042] 4. Prepare a 5wt% hydrochloric acid aqueous solution with a volume of 2.5L, dissolve 50g copper chloride and 50g barium chloride in the hydrochloric acid aqueous solution, and use it as impregnation solution B;

[0043] 5. Add the impregnated activated carbon obtained in step 3 into the impregnation solution B, impregnate at 80°C for 15 hours, and...

Embodiment 3

[0046] 1. The activated carbon is pretreated to remove the ash, and dried to constant weight at 120°C to obtain the pretreated activated carbon;

[0047] 2. Prepare a 12wt% hydrochloric acid aqueous solution with a volume of 2.0L, dissolve 80g of mercuric chloride and 100g of cesium chloride in the hydrochloric acid aqueous solution, and use it as impregnation solution A;

[0048] 3. Weigh 1 kg of pretreated activated carbon dried to constant weight and add it to impregnating solution A, soak at 80°C for 15 hours, take out the activated carbon carrier impregnated with active components, and dry at 120°C to constant weight;

[0049] 4. Prepare a 5wt% hydrochloric acid aqueous solution with a volume of 2.5L, dissolve 50g copper chloride and 50g barium chloride in the hydrochloric acid aqueous solution, and use it as impregnation solution B;

[0050] 5. Add the impregnated activated carbon obtained in step 3 into the impregnation solution B, impregnate at 80°C for 15 hours, and t...

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Abstract

The invention discloses a preparation method of a composite low solid mercury catalyst used for acetylene hydrochlorination. The preparation method comprises the steps of firstly dissolving mercury chloride and alkali chloride into a hydrochloric acid solution to prepare impregnation liquid A, dissolving a chloride assistant into the hydrochloric acid solution to prepare impregnation liquid B, sufficiently impregnating pretreated activated carbon in the impregnation liquid A, then sufficiently impregnating the impregnated activated carbon in the impregnation liquid B, and drying to prepare the composite low mercury catalyst. In the prepared composite low solid mercury catalyst, the loading amount of mercury chloride is 4-6.5wt%, the loading amount of alkali chloride is 0.5-10wt%, and the loading amount of the chloride assistant is 1-10wt%. According to the preparation method, two impregnation steps are adopted, wherein in the first impregnation step, mercury chloride is introduced to the surface of a carrier in a negative ion manner by adopting the co-impregnation method of a solid mercury agent and mercury chloride, the adsorption effect of mercury chloride of the low mercury catalyst can be effectively improved, the volatilization amount of mercury chloride can be reduced, and the stability of the catalyst can be improved; and in the second impregnation step, other active metal chloride is added, so that the composite low solid mercury catalyst with high stability and high activity can be obtained.

Description

technical field [0001] The invention relates to a composite low-mercury catalyst for hydrochlorination of acetylene and a preparation method thereof. Background technique [0002] Vinyl chloride is a monomer for preparing polyvinyl chloride (PVC) and its copolymers. It is one of the most important chemical products alongside ethylene and sodium hydroxide in the world, and is widely used in various fields of the national economy. China's PVC industry is developing rapidly. According to the domestic energy pattern of "poor oil, rich coal, and little gas", the production of acetylene hydrochlorination plays a major role. The mercuric chloride catalyst required by the acetylene hydrochlorination method accounts for 60% of the national mercury consumption. With the pressing measures for the prevention and control of mercury pollution at home and abroad and the depletion of domestic mercury resources, calcium carbide polyvinyl chloride enterprises are facing a severe test. [00...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/138C07C21/06C07C17/08
Inventor 李瑛唐浩东韩文锋刘化章
Owner ZHEJIANG UNIV OF TECH