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Method for preparing phenol from benzene through one-step process

A step method and phenol technology, applied in the field of phenol preparation, can solve the problems of high catalyst preparation cost, cumbersome catalyst production, and lack of commercialization, and achieve considerable industrial application prospects, improve production conditions, and low cost.

Inactive Publication Date: 2012-05-23
PETROCHINA CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the cumbersome preparation of these catalysts, the high cost of catalyst preparation and the long reaction time, they have not been commercialized.
Zhang Jin et al. (Chinese invention patent ZL2003101041091) used activated carbon as a catalyst, hydrogen peroxide as an oxidant, and glacial acetic acid as a solvent to obtain a maximum yield of 13% of phenol, but the reaction temperature was relatively high (60°C).

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] Take 100g of coal-based activated carbon, grind, sieve, and take 40-80 mesh. Fully wash with tap water to remove inorganic impurities such as dust on the surface of activated carbon. Then wash with distilled water 3 times to remove trace metal ions adsorbed on the surface of coal-based activated carbon. Put it in an oven and dry it at 110°C. Add 100g of water-washed coal-based activated carbon to a 500mL flask, add 250mL of 10mol / L HNO 3 The solution was connected to a condenser, heated to reflux in a water bath at 90°C, and the tail gas was absorbed with NaOH solution, and treated for 10 hours. The acid-treated activated carbon was fully washed with tap water until the pH remained constant, and then rinsed three times with distilled water. Vacuum filter, put into oven, and dry at 110°C. Weigh 3.5090g Fe 2 (SO 4 ) 3 In 50mL distilled water, prepare 0.175mol / L Fe 2 (SO 4 ) 3 solution, 15g of treated coal-based activated carbon was added thereto, allowed to stan...

Embodiment 2

[0022] Take 100g of coal-based activated carbon, grind, sieve, and take 40-80 mesh. Fully wash with tap water to remove inorganic impurities such as dust on the surface of activated carbon. Then wash with distilled water 3 times to remove trace metal ions adsorbed on the surface of coal-based activated carbon. Put it in an oven and dry it at 110°C. Add 100g of water-washed coal-based activated carbon to a 500mL flask, add 250mL of 12mol / L HNO 3 The solution was connected to a condenser, heated to reflux in a water bath at 90°C, and the tail gas was absorbed with NaOH solution, and treated for 10 hours. The acid-treated coal-based activated carbon was fully washed with tap water until the pH remained constant, and then rinsed three times with distilled water. Vacuum filter, put into oven, and dry at 110°C. Weigh 3.5090g Fe 2 (SO 4 ) 3 In 50mL distilled water, prepare 0.175mol / L Fe 2 (SO 4 ) 3 solution, 15g of treated coal-based activated carbon was added thereto, allo...

Embodiment 3

[0024] Take 100g of coal-based activated carbon, grind, sieve, and take 40-80 mesh. Fully wash with tap water to remove inorganic impurities such as dust on the surface of activated carbon. Then wash with distilled water 3 times to remove trace metal ions adsorbed on the surface of coal-based activated carbon. Put it in an oven and dry it at 110°C. Add 100g of water-washed coal-based activated carbon to a 500mL flask, add 250mL of 2mol / L HNO 3 The solution was connected to a condenser, heated to reflux in a water bath at 90°C, and the tail gas was absorbed with NaOH solution, and treated for 10 hours. The acid-treated coal-based activated carbon was fully washed with tap water until the pH remained constant, and then rinsed three times with distilled water. Vacuum filter, put into oven, and dry at 110°C. Weigh 3.5090g Fe 2 (SO 4 ) 3 In 50mL distilled water, prepare 0.175mol / L Fe 2 (SO 4 ) 3 solution, 15g of treated coal-based activated carbon was added thereto, allow...

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PUM

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Abstract

The invention relates to a method for preparing phenol from benzene through a one-step process. According to the method, a catalyst treats coal-based active carbon as a carrier and a ferric salt as an active component, and the carrier of the catalyst is processed according to the following steps: 1, adding 100g of the coal-based active carbon washed by water to a flask, adding 250ml of a nitric acid solution with the concentration of 2-12mol / L, connecting a condenser tube to the flask, carrying out reflux processing for 10h in a 25-90DEG C water bath, absorbing a tail gas with an NaOH or Na2CO3 solution, fully washing the coal-based active carbon with tap water until the pH value is unchanged, leaching the coal-based active carbon with distilled water three times, carrying out pumping filtration, and drying the coal-based active carbon in a 110DEG C constant temperature drying box; and 2, dipping the coal-based active carbon in 20-50mL of an aqueous Fe2(SO4)3 solution with the concentration of 0.04-0.20mol / L, laying them aside for 0.5-24h at room temperature, carrying out pumping filtration, and drying the coal-based active carbon in the 110DEG C constant temperature drying box. The catalyst has the advantages of high activity, high selectivity, high stability, production cost reduction, and product quality improvement.

Description

technical field [0001] The invention relates to a method for preparing phenol from benzene in one step. Background technique [0002] Phenol is an important basic organic chemical raw material and is widely used in industry. At present, the industrial production of phenol mainly adopts the process of cumene, namely: alkylation of benzene to obtain cumene, oxidation of cumene to obtain cumene peroxide, and decomposition of cumene peroxide to produce phenol. The reaction route is long, the reaction energy consumption is large, the phenol yield is low, there is an intermediate product (oxidation product of cumene) that is prone to explosion, and the by-product acetone of equimolar amount with phenol will be produced, and the demand of acetone is much higher than that of phenol. Smaller than phenol, so acetone disposal is a big problem. In addition, acid and a variety of organic reagents need to be added to the three-step reaction, resulting in waste of resources, inconvenient...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/053C07C39/04C07C37/60
CPCY02P20/52
Inventor 徐新良胡常伟徐亚荣李桂英李亚平祝良芳展江宏张丽
Owner PETROCHINA CO LTD
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