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Process for the preparation of 1,3-propanediol

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

Active Publication Date: 2018-04-06
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 preparing 1,3-propanediol is provided, which has a high yield of 1,3-propanediol and high selectivity

Method used

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  • Process for the preparation of 1,3-propanediol
  • Process for the preparation of 1,3-propanediol
  • Process for the preparation of 1,3-propanediol

Examples

Experimental program
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Effect test

Embodiment 1

[0025] The preparation of hydroformylation catalyst: the RhCl that contains 6.50gRh, contains 1.50gLi and contains 3.50gSn 3 ·3H 2 O, LiCl, and SnCl 2 2H 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 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 Rh content of the catalyst was measured by ICP to be 6.50 g / L, the Li content was 1.50 g / L, and the Sn content was 3.50 g / L.

[0026] Synthesis of 1,3-propanediol:

[0027] 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. 1.0MPa, then feed carbon monoxide and hydrogen until the pressure is 5.2MPa, increase the stir...

Embodiment 2

[0033] The preparation of hydroformylation catalyst: the RhCl that contains 6.50gRh, contains 1.50gLi and contains 3.50gTi 3 ·3H 2 O, LiCl, and TiCl 4 Fully mix and dissolve 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 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 Rh content of the catalyst was measured by ICP to be 6.50 g / L, the Li content was 1.50 g / L, and the Ti content was 3.50 g / L.

[0034] Synthesis of 1,3-propanediol:

[0035] 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. 1.0MPa, then feed carbon monoxide and hydrogen until the pressure is 5.2MPa, increase the stirring speed to...

Embodiment 3

[0051] The preparation of hydroformylation catalyst: the Rh(OAc) that contains 6.50gRh, contains 1.50gK and contains 3.50gGe 3 、K 2 SO 4 and GeCl 4 Fully mixed and dissolved in 10wt% acetic acid aqueous solution to obtain 400ml of impregnating solution, and the specific surface of 1.0L was 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 100° C. to obtain the catalyst. The Rh content of the catalyst was determined by ICP to be 6.50 g / L, the K content to be 1.50 g / L, and the Ge content to be 3.50 g / L.

[0052] Synthesis of 1,3-propanediol:

[0053] 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. 1.0MPa, then feed carbon monoxide and hydrogen until the pressure is 5.2MPa, increase the stirring speed to 800rpm, stir and heat ...

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Abstract

The present invention relates to the method for preparing 1.3-propylene glycol, mainly solves the problem that 1.3-propylene glycol catalyst activity and selectivity are lower in the prior art, by adopting the method for preparing 1.3-propylene glycol, 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 its mixture is the carrier, and the active component includes rhodium, alkali metal and the technical scheme of at least one metal element selected from IVA and IVB, which better solves the technical problem and can be used for the industrial production of 1.3-propylene glycol middle.

Description

technical field [0001] The present invention relates to a process for the preparation 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 Compan...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C29/128C07C31/20C07C67/293C07C69/14B01J23/62B01J23/58
Inventor 查晓钟杨运信
Owner CHINA PETROLEUM & CHEM CORP