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Alkyne selective hydrogenation catalyst as well as preparation method and application thereof

A technology for selective hydrogenation and catalyst, applied in the field of alkyne hydrogenation, can solve the problem of inability to obtain butadiene-rich products, avoid excessive hydrogenation and polymerization coke deposition process, save production costs, improve selectivity and life Effect

Pending Publication Date: 2022-02-22
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In the prior art, when dealing with the hydrogenation and removal of alkynes of C4 materials containing high concentrations of alkynes, all of them are based on noble metal Pd catalysts, and the alkyne content of the hydrogenation products is still as high as thousands of ppm or higher, and it is impossible to obtain lower butadiene rich product
In addition, the selectivity and stability of the hydrogenation catalysts disclosed in the prior art also need to be improved

Method used

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  • Alkyne selective hydrogenation catalyst as well as preparation method and application thereof
  • Alkyne selective hydrogenation catalyst as well as preparation method and application thereof
  • Alkyne selective hydrogenation catalyst as well as preparation method and application thereof

Examples

Experimental program
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Effect test

Embodiment 1-32

[0064] The alkyne selective hydrogenation catalyst of embodiment 1-32, each component is as shown in table 1, and its preparation process is:

[0065] Step A, first prepare a certain concentration of nickel nitrate solution, aluminum nitrate solution and IB group and / or IIB group metal nitrate solutions with deionized water respectively, and obtain a mixed solution after mixing the various solutions; then use deionized water to separate Prepare a solution of a certain concentration of rare earth metal nitrate, alkali metal and / or alkaline earth metal nitrate;

[0066] Step B. Control the temperature of the mixed solution to 70°C, add the precipitant ammonia water under vigorous stirring, adjust the pH value to about 8.5, react for 40 minutes, and age for 0.5 hours;

[0067] Step C, under vigorous stirring, add a solution containing rare earth compounds, a solution containing alkali metals and / or alkaline earth metal compounds and ammonia water as a precipitant to the mixed sol...

Embodiment 33

[0074] Step A, first prepare nickel nitrate solution, aluminum nitrate solution, copper nitrate solution, lanthanum nitrate solution, lithium nitrate solution with deionized water respectively;

[0075] Step B. Mix all the above solutions, control the temperature of the mixed solution to 70°C, add the precipitant ammonia water under vigorous stirring, adjust the pH value to about 8.5, react for 40 minutes, and age for 1.5 hours; filter the filter cake, and then use it The catalyst was prepared by washing with ion water, molding, and calcining at 450°C for 4 hours.

Embodiment 34

[0077] Except that the temperature of the mixed solution is controlled to be 45° C. in step B, the others are the same as in Example 1.

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Abstract

The invention discloses an alkyne selective hydrogenation catalyst, which comprises the following components: nickel oxide, aluminum oxide, IB group and / or IIB group metal oxide, rare earth metal oxide and alkali metal and / or alkaline earth metal oxide. The catalyst is high in activity, good in selectivity and excellent in stability, and is particularly suitable for butadiene extraction tail gas, namely a reaction process for selectively hydrogenating, removing alkyne and recovering butadiene from a butadiene-rich C4 material with high alkyne content. The invention also discloses a preparation method and application of the selective hydrogenation catalyst.

Description

technical field [0001] The present invention relates to a catalyst for selective hydrogenation of alkynes and its preparation method and application, especially a catalyst which can be used for selective hydrogenation of butadiene-rich residual material which has concentrated alkyne after extraction of butadiene and its preparation method , and the selective hydrogenation method of the material belong to the technical field of alkyne hydrogenation. Background technique [0002] The butadiene extraction unit of petrochemical enterprises will by-produce a large amount of butadiene tail gas, in which the content of dienes and alkynes is very high, generally containing about 30-40wt% of dienes, about 10-20wt% of carbon tetra-alkynes, individual The alkyne content in the butadiene tail gas of the refinery is even as high as 50wt%. Recovering the butadiene rich in the extraction tail gas can greatly improve the total butadiene recovery rate of the butadiene extraction device, and...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83B01J23/89B01J37/03B01J37/08C07C7/167C07C11/167
CPCB01J23/83B01J23/8946B01J23/002B01J37/031B01J37/088C07C7/167B01J2523/00C07C2523/83C07C2523/89C07C11/167B01J2523/11B01J2523/17B01J2523/3706B01J2523/847B01J2523/23B01J2523/3712B01J2523/18
Inventor 熊凯杜周张富春任玉梅
Owner CHINA PETROLEUM & CHEM CORP