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Method for preparing benzalcohol by hydrogenation of hydrogen peroxide cumene

A technology for preparing cumene hydrogen peroxide and benzyl alcohol, which is applied in chemical instruments and methods, isomerization preparation, hydroxyl compound preparation, etc., can solve problems such as poor industrial practicability, harsh operation skills, and difficulty in treating wastewater. , to avoid pollution and solve stability problems

Active Publication Date: 2009-01-21
CHINA PETROLEUM & CHEM CORP +1
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Problems solved by technology

[0003] Theoretically speaking, there are multiple synthetic methods of DCP, such as US 3829503, DE2016108, etc. These methods all have the following disadvantages: the one is multi-step reaction and each step is intermittent production; the 2nd, the synthetic methods of these DCP all use Cumyl hydroperoxide (abbreviated as CHP) is used as a reaction intermediate product, and CHP belongs to aralkyl hydroperoxide, which is very unstable to acid, alkali, heat, reducing agent, heavy metal ion, etc. All th

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  • Method for preparing benzalcohol by hydrogenation of hydrogen peroxide cumene
  • Method for preparing benzalcohol by hydrogenation of hydrogen peroxide cumene
  • Method for preparing benzalcohol by hydrogenation of hydrogen peroxide cumene

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[0054] Example

[0055] Combine the process of the present invention figure 1 The production process is described as follows:

[0056] The reaction raw material from line 6 is mixed with the circulating material from circulating line 4 in the fluidized bed reactor, and then enters the material heater 16 through line 5, where it is heated to 30-50°C and then enters the fluidized bed reactor 1. The new hydrogen sent from line 13 is mixed with the circulating hydrogen sent from line 12 and then enters into hydrogen heater 19 through line 14, where it is heated to 30-50°C and then enters into gas distribution 18, and then enters after being distributed by gas distributor To the reaction zone of fluidized reactor 1. A hydrogenation catalyst is installed in the reactor 1, and the hydrogenation reaction is carried out under suitable reaction conditions. The reacted liquid comes out of line 2, a part of the liquid is circulated back to reactor 1 through line 4, and the other part is sent ...

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Abstract

The invention relates to a method for preparing benzoic alcohol through hydrogenation of cumene hydroperoxide. The method comprises the following steps that cumene hydroperoxide and hydrogen pass through a reactor containing hydrogenation catalyst; the reactor adopts an ebullated bed reactor of a high-efficiency mass transfer and heat transfer reactor; a reaction raw material is fed in from the bottom of the reactor; and materials are discharged from the top of the reactor after reaction, and hydrogen is recycled after deoxidation. Through adopting strong mass transfer and heat transfer reactors such as the ebullated bed reactor to carry out hydro catalytic reduction for CHP, the method solves the problems of reaction mass transfer and heat transfer during reaction; a deoxidation reactor is arranged on a hydrogen circulation line, so the method solves the problem of stability during reaction. Moreover, the process of the method can realize continuous production, and does not discharge the three wastes during production, thereby preventing environmental pollution.

Description

technical field [0001] The present invention relates to a kind of method of producing alcohol by peroxide, specifically the method for preparing benzyl alcohol by hydrogenation of cumene hydroperoxide. Background technique [0002] Dicumyl peroxide (DCP for short) is a commonly used symmetrical di-tertiary alkyl peroxide. It is mainly used as a crosslinking agent for polyethylene, chlorinated polyethylene, and polystyrene, and secondly as a polymerization initiator. agent and blowing agent for ethylene-vinyl acetate copolymer. [0003] Theoretically speaking, there are multiple synthetic methods of DCP, such as US 3829503, DE2016108, etc. These methods all have the following disadvantages: the one is multi-step reaction and each step is intermittent production; the 2nd, the synthetic methods of these DCP all use Cumyl hydroperoxide (abbreviated as CHP) is used as a reaction intermediate product, and CHP belongs to aralkyl hydroperoxide, which is very unstable to acid, alkal...

Claims

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Application Information

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IPC IPC(8): C07C33/22C07C29/56C07C29/00
Inventor 艾抚宾王海波勾连科宋丽芝张淑梅
Owner CHINA PETROLEUM & CHEM CORP
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