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Method for synthesizing 1,3-propanediol through hydroformylation of vinyl acetate

A technology for vinyl acetate hydroformyl and acetoxypropanol, which is applied in the field of vinyl acetate hydroformylation to synthesize 1,3-propanediol, can solve the problems of low yield and selectivity of propylene glycol, and achieves improved activity and stability Effect

Active Publication Date: 2017-12-15
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 this invention is the low yield and selectivity of 1,3-propanediol, and a new method for the synthesis of 1,3-propanediol by hydroformylation of vinyl acetate is provided, which has the advantages of 1,3-propanediol The characteristics of high yield and high selectivity of propylene glycol

Method used

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  • Method for synthesizing 1,3-propanediol through hydroformylation of vinyl acetate
  • Method for synthesizing 1,3-propanediol through hydroformylation of vinyl acetate
  • Method for synthesizing 1,3-propanediol through hydroformylation of vinyl acetate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Preparation of hydroformylation catalyst: Co containing 8.40gCo, 1.70gTe and 3.10gCr 2 (CO) 8 , ammonium tellurate ((NH 4 ) 2 TeO 4 ) and Cr(OAc) 3 ·6H 2 O is 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 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 Co content of the catalyst was determined by ICP to be 8.40 g / L, the Te content was 1.70 g / L, and the Cr content was 3.10 g / L.

[0029] Synthesis of 1,3-propanediol:

[0030]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 12.0MPa, increase th...

Embodiment 2

[0036] Preparation of hydroformylation catalyst: Co containing 8.40gCo, 1.70gTe and 3.10gSr 2 (CO) 8 , ammonium tellurate ((NH 4 ) 2 TeO 4 ) and Sr(OA C ) 2 0.5H 2 O is 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 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 Co content of the catalyst was determined by ICP to be 8.40 g / L, the Te content was 1.70 g / L, and the Sr content was 3.10 g / L.

[0037] Synthesis of 1,3-propanediol:

[0038] 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 12.0MPa, increa...

Embodiment 3

[0054] The preparation of hydroformylation catalyst: the Co(OAc) that contains 7.00gCo, contains 0.50gB and contains 1.00gCr 2 4H 2 O, ammonium pentaborate ((NH 4 )B 5 o 8 ·8H 2 O) and CrCl 3 ·6H 2 O is fully mixed and dissolved in a concentration of 10wt% acetic acid aqueous solution 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 was measured by ICP and ICP-MS to be 7.00 g / L, the B content was 0.50 g / L, and the Cr content was 1.00 g / L.

[0055] Synthesis of 1,3-propanediol:

[0056] 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 un...

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Abstract

The invention relates to a method for synthesizing 1,3-propanediol by hydroformylation of vinyl acetate, which mainly solves the problem of low catalyst activity and selectivity of 1,3-propanediol in the prior art. By adopting the preparation method of 1,3-propanediol, The method comprises the following steps: hydroformylation of vinyl acetate to obtain 3-acetoxy propionaldehyde; hydrogenation of 3-acetoxy propionaldehyde to obtain 3-acetoxypropanol; hydrolysis of 3-acetoxypropanol to obtain 1,3- Propylene glycol; the hydroformylation catalyst uses SiO2, Al2O3 or a mixture thereof as a carrier, and the active component includes at least one selected from iron series elements, at least one selected from metalloid elements, and selected from VIB and alkaline earth metals The technical scheme of at least one metal element solves this technical problem better, and can be used in the industrial production of 1,3-propylene glycol.

Description

technical field [0001] The invention relates to a method for synthesizing 1,3-propanediol through hydroformylation of vinyl acetate. 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 Compa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C31/20C07C29/09C07C69/14C07C67/293B01J31/34B01J31/28B01J27/057B01J23/86B01J23/881B01J23/887B01J23/888
Inventor 查晓钟杨运信
Owner CHINA PETROLEUM & CHEM CORP