Alpha, alpha-dimethyl benzyl alcohol hydrogenolysis catalyst as well as preparation method and application thereof

A technology of dimethylbenzyl alcohol and a catalyst, which is applied in the field of CHP production of propylene oxide, can solve problems such as difficult operation, poor catalyst stability, environmental pollution, etc., and achieves the advantages of reducing operation difficulty, improving selectivity, and reducing separation cost. Effect

Pending Publication Date: 2022-05-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] Aiming at the problems of poor catalyst stability, serious environmental pollution, easy hydrogenation of by-product acetophenone and difficult operation in the existing DMBA hydrogenolysis technology in the CHP process of producing propylene oxide, the present invention provides an α,α-di A catalyst for the hydrogenolysis of methyl benzyl alcohol, in which an appropriate amount of Si is deposited on the surface of the catalyst active component Pd to effectively inhibit the excessive hydrogenation of α,α-dimethyl benzyl alcohol and the hydrogenation of acetophenone in organic materials, thereby effectively Improve the selectivity of cumene, control the content of ethylbenzene in the product, reduce the cost of separation in the later stage, and the obtained α,α-dimethylbenzyl alcohol hydrogenolysis catalyst is used in the hydrogenolysis of α,α-dimethylbenzyl alcohol to prepare cumene Good stability and high industrial application value

Method used

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  • Alpha, alpha-dimethyl benzyl alcohol hydrogenolysis catalyst as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0069] Fill 20mL (12.0g) catalyst PreC2 in comparative example 1 in the fixed-bed reaction tube, when 250 ℃, feed 100ppmSiH respectively 4 / H 2 The mixed gas was mixed for 5 minutes to obtain the catalyst SiC1, the main composition of which is shown in Table 1.

Embodiment 2

[0071] Fill 20mL (12.0g) catalyst PreC2 in comparative example 1 in the fixed-bed reaction tube, when 250 ℃, feed 100ppmSiH respectively 4 / H 2 The mixed gas was mixed for 30 minutes to obtain the catalyst SiC2, the main composition of which is shown in Table 1.

Embodiment 3

[0073] Fill 20mL (12.0g) catalyst PreC2 in comparative example 1 in the fixed-bed reaction tube, when 250 ℃, feed 100ppmSiH respectively 4 / H 2 Mixed gas for 2h, the catalyst SiC3 is obtained, the main composition is shown in Table 1.

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Abstract

The invention discloses an alpha, alpha-dimethyl benzyl alcohol hydrogenolysis catalyst and a preparation method and application thereof, the catalyst comprises a carrier, metal palladium loaded on the carrier and a silicon element loaded on the metal palladium, and the weight content ratio of the silicon element to the metal palladium is (0.1-8): 100. When the catalyst is applied to the hydrogenolysis process of alpha, alpha-dimethyl benzyl alcohol containing acetophenone, excessive hydrogenation of hydrogenolysis of alpha, alpha-dimethyl benzyl alcohol and hydrogenation of acetophenone in organic materials can be effectively inhibited, so that the selectivity of isopropyl benzene is effectively improved, the content of ethylbenzene in a product is controlled, and the later separation cost is reduced; the isopropylbenzene prepared by hydrogenolysis of alpha-dimethyl benzyl alcohol is good in stability and has a relatively high industrial application value.

Description

technical field [0001] The invention relates to a CHP process for preparing propylene oxide, in particular to the hydrogenolysis of propylene oxidation unit products. Background technique [0002] Propylene oxide (PO), as a downstream product of propylene, is an important organic chemical product and can be used to produce polyether polyols, the precursors of polyurethane materials. The CHP legal PO process developed by Japan Sumitomo Chemical Co., Ltd. has no joint products, no pollution to the environment, and less investment. It is an environmentally friendly clean production process. The new CHP PO process includes cumene oxidation, propylene epoxidation, α,α-dimethylbenzyl alcohol hydrogenolysis (DMBA) and other processes. In the propylene oxidation unit, cumene hydroperoxide oxidizes propylene to generate PO and α,α-Dimethylbenzyl alcohol, and a small amount of acetophenone by-product. [0003] Chinese patent CN104230643A uses two kinds of DMBA hydrogenolysis catalys...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/44C07C1/20C07C15/085
CPCB01J23/44C07C1/20C07C15/085Y02P20/52
Inventor 吕宇皓刘仲能赵多马文迪王燕波
Owner CHINA PETROLEUM & CHEM CORP
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