Zinc catalyst for catalyzing acetylene hydration reaction and preparation method of zinc catalyst

A zinc catalyst and acetylene hydration technology, which is applied in the preparation of carbon-carbon triple bond hydration, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve the problems of high energy consumption and low selectivity, and achieve small particles and high selectivity , the effect of less by-products

Pending Publication Date: 2018-12-14
SHIHEZI UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] At present, the hydration reaction of acetylene is basically carried out at a relatively high temperature, and there are problems such as high energy consumption and low selectivity.

Method used

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  • Zinc catalyst for catalyzing acetylene hydration reaction and preparation method of zinc catalyst
  • Zinc catalyst for catalyzing acetylene hydration reaction and preparation method of zinc catalyst
  • Zinc catalyst for catalyzing acetylene hydration reaction and preparation method of zinc catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0037] The specific operation steps are as follows:

[0038] (1) Preparation of molecular sieve precursor solution: weigh 5.2 g of cetyltrimethylammonium bromide and 2.4 g of sodium hydroxide, and completely dissolve them in 200.0 mL of deionized water, mix and heat to 35 ° C after complete dissolution, Add 19.8 g of ethyl orthosilicate, and continue stirring for 1 h to obtain a molecular sieve precursor solution.

[0039] (2) Preparation of modified carrier: under vigorous stirring, 8 g of n-butyl titanate was added dropwise to the molecular sieve precursor solution, and after uniform stirring, a modified molecular sieve precursor solution was obtained.

[0040] The modified molecular sieve precursor solution was heated, stirred for 4 hours, then washed with water for several times until the pH value was neutral, dried at 60°C for 12 hours, calcined in a nitrogen tube furnace at 500°C for 5 hours, and then calcined in a muffle furnace at 500°C 6h, the modified molecular siev...

Embodiment 2

[0050] The operating steps of Example 2 are the same as those of Example 1, except that the amount of n-butyl titanate added is 1 g.

[0051] During the activity test, when the reaction temperature is 100-400°C, C 2 h 2 The flow rate is 3.4ml / min, H 2 The flow rate of O is 0.01g / min, and the space velocity is adjusted to 90h -1 Under certain conditions, the conversion rate of acetylene reaches the highest value of 78%, and the selectivity of acetaldehyde is greater than 75%.

Embodiment 3

[0053] The operation steps of Example 3 are the same as those of Example 1, except that the amount of n-butyl titanate added is 1.34 g.

[0054] During the activity test, when the reaction temperature is 100-400°C, C 2 h 2 The flow rate is 3.4ml / min, H 2 The flow rate of O is 0.01g / min, and the space velocity is adjusted to 90h -1 Under certain conditions, the conversion rate of acetylene reaches the highest value of 75%, and the selectivity of acetaldehyde is greater than 85%.

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Abstract

The invention relates to a zinc catalyst for catalyzing an acetylene hydration reaction and a preparation method of the zinc catalyst. The method for preparing the zinc catalyst for catalyzing an acetylene hydration reaction comprises the following steps of (1) preparing a modified carrier: adding a modifying agent to a molecular sieve precursor liquid, performing uniform mixing, performing filtering, performing drying, performing calcining and performing roasting to obtain the modified carrier; (2) preparing the catalyst precursor salt liquid: enabling zinc salt to completely dissolve in water to obtain the catalyst precursor salt liquid; and (3) preparing the catalyst: dropwise adding the catalyst precursor salt liquid to the modified carrier, performing immersing for 12h, and performingdrying to obtain the zinc catalyst. According to the zinc catalyst for catalyzing an acetylene hydration reaction and the preparation method of the zinc catalyst, the preparation cycle is short, andthe operation is simple; and the prepared zinc catalyst is a non-mercury catalyst for the acetylene hydration reaction, so that mercury pollution to environment can be avoided. The prepared zinc catalyst is high in activity and high in selectivity in the acetylene hydration reaction.

Description

technical field [0001] The invention belongs to the field of catalysts, in particular to a zinc catalyst for catalyzing the hydration reaction of acetylene and a preparation method thereof. Background technique [0002] Acetaldehyde is an important fine chemical intermediate and an important basic organic synthesis intermediate for the production of acetic acid, acetic anhydride, butyraldehyde, butanol, etc. Since the industrial production of acetaldehyde by hydration of acetylene in 1961, acetylene has become an important raw material in coal-based chemicals. However, with the vigorous development of petrochemical industry, the process of hydrating acetylene to produce acetaldehyde was gradually replaced by the process of oxidizing ethylene to produce acetaldehyde. However, due to China's huge coal reserves, and the continuous improvement of the calcium carbide acetylene production process, the cost has gradually decreased, and the product quality has continued to improve....

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/04C07C45/26C07C47/06
CPCB01J29/041B01J2229/18C07C45/26C07C47/06
Inventor 代斌王琴琴朱明远
Owner SHIHEZI UNIVERSITY
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