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Preparation method of styrene

A technology of styrene and alkali lignin, which is applied in chemical instruments and methods, chemical recovery, hydrocarbons, etc., can solve the problems of tall and large distillation towers, high reflux ratio, and large energy consumption, and achieve low production cost and high separation process The effect of simplifying and reducing production costs

Inactive Publication Date: 2017-01-04
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because styrene and ethylbenzene have similar boiling points (145°C and 136°C, respectively), their separation requires a tall distillation column and a high reflux ratio, which consumes a lot of energy

Method used

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  • Preparation method of styrene
  • Preparation method of styrene

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] (1) Add 0.4g alkali lignin, 0.01g H-GN catalyst, 4g 30wt% hydrogen peroxide aqueous solution (m 碱木质素 :m H-GN催化剂 =40:1, m 碱木质素 :m 过氧化氢水溶液 =1:10), add 0.4mol / L NaOH solution to adjust the pH value of the reaction solution to 13; stir the reaction in a constant temperature oil bath at 60°C for 1h, and the reaction mixture becomes homogeneous and black after heating;

[0033] (2) After the reaction is completed, centrifuge, and the centrifuged solid is washed with deionized water, centrifuged three times, dried in an oven at 60°C for 12 hours, and the H-GN catalyst is recovered for recycling; the obtained supernatant is acidified to pH with concentrated hydrochloric acid It is 2, after static precipitation, centrifuge and filter the mixture, the obtained solid is dried in an oven at 100°C to recover undegraded alkali lignin, the obtained supernatant is extracted with ethyl acetate for 3 times, and rotary evaporated under reduced pressure in an oil bath at 55°C The drople...

Embodiment 2

[0037] (1) Add 0.4g alkali lignin, 0.01g H-GN catalyst, 4g 30wt% hydrogen peroxide aqueous solution (m 碱木质素 :m H-GN催化剂 =40:1, m 碱木质素 :m 过氧化氢水溶液 =1:10), add 0.4mol / L NaOH solution to adjust the pH value of the reaction solution to 13; stir and react in a constant temperature oil bath at 60°C for 5h, the reaction mixture becomes homogeneous and black after heating;

[0038] (2) After the reaction is completed, centrifuge, and the centrifuged solid is washed with deionized water, centrifuged three times, dried in an oven at 60°C for 12 hours, and the H-GN catalyst is recovered for recycling; the obtained supernatant is acidified to pH with concentrated hydrochloric acid It is 2, after static precipitation, centrifuge and filter the mixture, the obtained solid is dried in an oven at 100°C to recover undegraded alkali lignin, the obtained supernatant is extracted with ethyl acetate for 3 times, and rotary evaporated under reduced pressure in an oil bath at 55°C The droplet produ...

Embodiment 3

[0041] (1) Add 0.4g alkali lignin, 0.01g H-GN catalyst, 4g 30wt% hydrogen peroxide aqueous solution (m 碱木质素 :m H-GN催化剂 =40:1, m 碱木质素 :m 过氧化氢水溶液 =1:10), add 0.4mol / L NaOH solution to adjust the pH of the reaction solution to 13; stir and react in a constant temperature oil bath at 60°C for 9 hours, the reaction mixture becomes homogeneous and black after heating;

[0042] (2) After the reaction is completed, centrifuge, and the centrifuged solid is washed with deionized water, centrifuged three times, dried in an oven at 60°C for 12 hours, and the H-GN catalyst is recovered for recycling; the obtained supernatant is acidified to pH with concentrated hydrochloric acid It is 2, after static precipitation, centrifuge and filter the mixture, the obtained solid is dried in an oven at 100°C to recover undegraded alkali lignin, the obtained supernatant is extracted with ethyl acetate for 3 times, and rotary evaporated under reduced pressure in an oil bath at 55°C The droplet produc...

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Abstract

The invention discloses a preparation method of styrene. The method comprises the following steps: (1) pyrolysis of alkali lignin; and (2) separation and purification of target product. The raw material lignin is a renewable resource, and has the advantages of wide sources, stable supply and lower cost. The method has the advantages of simple technique, low facility requests and low production cost, and the H-GN catalyst is recyclable. The method has the characteristics of low reaction temperature and low required energy consumption, and can effectively lower the production cost.

Description

technical field [0001] The invention relates to the technical field of styrene preparation, in particular to a method for preparing styrene. Background technique [0002] Styrene is an important basic organic chemical raw material and is a colorless, oily liquid. Industrially, styrene is mainly used to manufacture materials such as polystyrene resin, ion exchange resin, synthetic resin coating, unsaturated polyester resin and insulator. These materials have important uses in industrial sectors such as automobile manufacturing, textiles, building materials, and light industry. There are three main routes for industrial mass production of styrene: one is the gas-phase catalytic dehydrogenation process of ethylbenzene, using ethylbenzene as raw material; the other is the by-product when propylene and ethylbenzene are peroxidized to produce propylene oxide; It is recovered by extraction and distillation from pyrolysis gasoline. Ethylbenzene dehydrogenation is the most commonl...

Claims

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Application Information

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IPC IPC(8): C07C4/00C07C15/46
CPCC07C4/00C07C15/46Y02P20/584
Inventor 陈砺余素庄严宗诚
Owner SOUTH CHINA UNIV OF TECH