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Method for preparing n-pentene from n-pentanol

A technology of n-pentene and n-pentanol, which is applied in the field of n-pentene preparation, can solve the problems that n-pentene technology is seldom introduced, so as to improve the conversion rate of n-pentene, improve the selectivity of n-pentene, and improve the n-pentene The effect of high conversion rate of alcohol

Active Publication Date: 2020-01-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] Existing literature has little introduction on the technology of n-butanol dehydration to prepare n-pentene

Method used

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  • Method for preparing n-pentene from n-pentanol
  • Method for preparing n-pentene from n-pentanol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Weigh 200 grams of alumina (its total pore volume is 0.94 cm 3 / gram, the pore volume of the pore diameter10 nanometers accounts for 74.7% of the total pore volume), 60 grams of silica sol, and 12 grams of squash powder in the kneader Kneaded for 30 minutes, added 200 ml of 5% nitric acid solution, kneaded for another 10 minutes, then extruded, dried at 110°C for 10 hours, and activated in a muffle furnace at 650°C for 8 hours to obtain catalyst A. The molar ratio of catalyst alumina and silica is shown in Table 1. The catalyst performance evaluation test was carried out on a fixed-bed tubular reactor (Ф25×500 mm stainless steel), and the catalyst loading was 10 ml. The experimental conditions and reaction results are shown in Table 2.

Embodiment 2

[0027] Weigh 200 grams of alumina (its total pore volume is 0.80 cm 3 / gram, the pore volume of the pore diameter10 nanometers accounts for 64.9% of the total pore volume), 59 grams of white carbon black, and 12 grams of squid powder in a kneader Kneading in the medium for 30 minutes, adding 250 ml of 5% nitric acid solution, kneading for another 10 minutes, extruding, drying at 120°C for 5 hours, and activation in a muffle furnace at 550°C for 16 hours to obtain catalyst B. The molar ratio of catalyst alumina and silica is shown in Table 1. The catalyst performance evaluation test was carried out on a fixed-bed tubular reactor (Ф25×500 mm stainless steel), and the catalyst loading was 10 ml. The experimental conditions and reaction results are shown in Table 2.

Embodiment 3

[0029] Weigh 200 grams of alumina (its total pore volume is 1.12 cm 3 / gram, the pore volume of the pore diameter10 nanometers accounts for 59.5% of the total pore volume), 30 grams of silica sol, and 12 grams of squash powder in the kneader Kneaded for 30 minutes, added 220 ml of 5% nitric acid solution, kneaded for another 10 minutes, then extruded, dried at 90°C for 15 hours, and activated in a muffle furnace at 500°C for 18 hours to obtain catalyst C. The molar ratio of catalyst alumina and silica is shown in Table 1. The catalyst performance evaluation test was carried out on a fixed-bed tubular reactor (Ф25×500 mm stainless steel), and the catalyst loading was 10 ml. The experimental conditions and reaction results are shown in Table 2.

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Abstract

The invention relates to a method for preparing n-pentene by n-amyl alcohol. The method comprises the steps of taking n-amyl alcohol as a raw material, contacting the raw material with a catalyst, and performing a reaction to generate n-pentene, wherein the catalyst comprises alumina and silicon oxide; the total pore volume of alumina is 0.7-1.2cm<3> / g; the pore volume with the pore diameter less than 10nm accounts for 10-50% of the total pore volume; the pore volume with the pore diameter greater than 10nm accounts for 50-90% of the total pore volume. The method can be used in industrial production of n-pentene prepared by n-amyl alcohol.

Description

technical field [0001] The invention relates to a method for preparing n-pentene, in particular to a method for preparing n-pentene from n-pentanol. Background technique [0002] N-pentene is a colorless and volatile liquid, soluble in ethanol and insoluble in water. It is a high value-added fine chemical intermediate, used for the production of pesticide propazolin intermediates, carbonylation to produce n-hexaldehyde, N-hexanol, n-hexanoic acid, and for polymer material modification. N-pentene can be obtained by dehydrating n-pentanol under the action of a catalyst. [0003] Patent CN101492333A discloses a method for dehydrating alcohols to olefins, including contacting alcohol raw materials with a catalyst, wherein the catalyst used includes the following components in weight percentage: a) 30-90% silicon-aluminum molar ratio Si / Al is less than 100 of UFI zeolite; b) the balance of alumina. When used for dehydration of 3-methyl-1-butanol to produce 3-methyl-1-butene, t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/10C07C1/24B01J21/12
Inventor 徐菁金照生吕建刚孙兰萍黄祖娟金萍周海春
Owner CHINA PETROLEUM & CHEM CORP