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Method for the synthesis of 1,3‑propanediol

A technology selected from propylene glycol, which is applied in the field of 1,3-propanediol synthesis, can solve the problems of low yield and selectivity of propylene glycol, and achieve the effect of improving activity and stability

Active Publication Date: 2017-11-21
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The technical problem to be solved by the present invention is the problem of low yield and selectivity of 1,3-propanediol, and a new method for 1,3-propanediol synthesis is provided, which has a high yield of 1,3-propanediol and high selectivity

Method used

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  • Method for the synthesis of 1,3‑propanediol
  • Method for the synthesis of 1,3‑propanediol
  • Method for the synthesis of 1,3‑propanediol

Examples

Experimental program
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Effect test

Embodiment 1

[0030] Preparation of hydroformylation catalyst: Co containing 8.50gCo, containing 2.10gLi and containing 2.80gBi 2 (CO) 8 , LiCl and bismuth subsalicylate (C 7 h 5 BiO 4 ) fully mixed and dissolved in an aqueous acetic acid solution with a concentration of 10wt%, to obtain 400ml of impregnation solution, and the specific surface of 1.0L was 168m 2 / g, spherical SiO with a pore volume of 0.94 and a diameter of 5.6 mm 2 The carrier was immersed in the above impregnating solution, left to stand for 3 hours and dried at 100° C. to obtain the catalyst. The Co content of the catalyst measured by ICP is 8.50 g / L, the Li content is 2.10 g / L, and the Bi content is 2.80 g / L.

[0031] Synthesis of 1,3-propanediol:

[0032] Step (1): Add 2.50 mol of toluene, 0.02 mol of hydroformylation main catalyst, 0.20 mol of triphenylphosphine and 1.65 mol of vinyl acetate into a 1L titanium reactor. 2.0MPa, then feed carbon monoxide and hydrogen until the pressure is 12.4MPa, increase the stir...

Embodiment 2

[0038] The preparation of hydroformylation catalyst: the Co containing 8.50gCo, containing 2.10gLi and containing 2.80gAu 2 (CO) 8 , LiCl and ammonium tetrachloroaurate (NH 4 AuCl 4 2H 2 O) fully mixed and dissolved in the acetic acid aqueous solution with a concentration of 10wt%, to obtain 400ml of impregnation solution, and the specific surface of 1.0L was 168m 2 / g, spherical SiO with a pore volume of 0.94 and a diameter of 5.6mm 2 The carrier was immersed in the above impregnating solution, left to stand for 3 hours and dried at 100° C. to obtain the catalyst. The Co content of the catalyst was determined by ICP to be 8.50 g / L, the Li content was 2.10 g / L, and the Au content was 2.80 g / L.

[0039] Synthesis of 1,3-propanediol:

[0040] Step (1): Add 2.50 mol of toluene, 0.02 mol of hydroformylation main catalyst, 0.20 mol of triphenylphosphine and 1.65 mol of vinyl acetate into a 1L titanium reactor. 2.0MPa, then feed carbon monoxide and hydrogen until the pressure...

Embodiment 3

[0056] The preparation of hydroformylation catalyst: the Co(OAc) that contains 7.00gCo, contains 0.50gNa and contains 1.00gBi 2 4H 2 O, Na 2 O and (BiO) 2 CO 3 0.5H 2 O is fully mixed and dissolved in an aqueous hydrochloric acid solution with a concentration of 8wt% to obtain 400ml of impregnation solution, and the specific surface of 1.0L is 200m 2 / g, spherical Al with a pore volume of 1.00 and a diameter of 5.6mm 2 o 3 The carrier was immersed in the above impregnating solution, left to stand for 3 hours and dried at 80° C. to obtain the catalyst. The Co content of the catalyst measured by ICP was 7.00 g / L, the Na content was 0.50 g / L, and the Bi content was 1.00 g / L.

[0057] Synthesis of 1,3-propanediol:

[0058] Step (1): Add 2.50 mol of toluene, 0.02 mol of hydroformylation main catalyst, 0.20 mol of triphenylphosphine and 1.65 mol of vinyl acetate into a 1L titanium reactor. 2.0MPa, then feed carbon monoxide and hydrogen until the pressure is 12.4MPa, increas...

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Abstract

The present invention relates to the method for 1.3-propanediol synthesis, mainly solves the problem that 1.3-propanediol catalyst activity and selectivity are lower in the prior art, by adopting the method for 1.3-propanediol synthesis, comprises the following steps: Acylation to obtain 3‑acetoxypropionaldehyde; hydrogenation of 3‑acetoxypropionaldehyde to obtain 3‑acetoxypropanol; alcoholysis of 3‑acetoxypropanol to obtain 1.3‑propanediol; hydroformylation catalyst using SiO2 , Al2O3 or a mixture thereof as a carrier, and the active component includes at least one iron element, an alkali metal element and at least one metal element selected from VA and IB, which better solves the technical problem , can be used in the industrial production of 1.3‑propylene glycol.

Description

technical field [0001] The present invention relates to a process for the synthesis of 1,3-propanediol. Background technique [0002] 1,3-Propanediol (1.3-PDO) is an important chemical raw material, mainly used in the synthesis of plasticizers, detergents, preservatives, emulsifiers, and also used in food, cosmetics and pharmaceutical industries. Because it is an important polyester fiber monomer, its main use is as a monomer and terephthalic acid to synthesize a new type of polyester material, polytrimethylene terephthalate (PTT). [0003] The preparation methods of 1,3-propanediol include ethylene oxide one-step method, ethylene oxide two-step method, acrolein hydration method, acetaldehyde-formaldehyde condensation method, acrylate method, biological method, vinyl acetate hydroformylation, etc. At present, the industrialized production method of 1.3-PDO is chemical synthesis, and the international market is mainly monopolized by Degussa Company of Germany, Shell Company ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C31/20C07C29/128B01J23/843B01J23/89B01J23/78
Inventor 查晓钟杨运信
Owner CHINA PETROLEUM & CHEM CORP