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Method for preparing vinyl acetate

A technology of vinyl acetate and diethylene acetate, which is applied in the preparation of carboxylic acid esters, chemical instruments and methods, and the preparation of organic compounds, can solve the problems of low selectivity and low yield of vinyl acetate, and achieve increased yield. efficiency and selectivity, and the effect of improving activity and stability

Active Publication Date: 2016-05-18
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 vinyl acetate yield and low selectivity, and a new method for preparing vinyl acetate is provided, which has the characteristics of high vinyl acetate yield and high selectivity

Method used

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  • Method for preparing vinyl acetate
  • Method for preparing vinyl acetate
  • Method for preparing vinyl acetate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] The preparation of carbonylation catalyst: the Co(OAc) that contains 8.98gCo, contains 2.75gLa and contains 3.25gZn 2 4H 2 O, La(OAc) 3 ·5H 2 O and zinc citrate (Zn 3 (C 6 h 5 o 7 ) 2 2H 2 O) fully mixed and dissolved in hydrochloric acid with a concentration of 8wt%, to obtain 400ml of impregnation solution, the specific surface of 1.0L was 165m2 / g, spherical SiO with a pore volume of 0.98 and a diameter of 5.6 mm 2 The carrier was immersed in the above impregnating solution, left to stand for 2 hours and dried at 100° C. to obtain the catalyst. The carbonylation catalyst was analyzed by ICP, and the Co content was 8.98g / L, the La content was 2.75g / L, and the Zn content was 3.25g / L.

[0029] Synthesis of vinyl acetate:

[0030] Step (1): Add 1.5 mol of acetic acid, 0.05 mol of carbonylation catalyst, 0.10 mol of methyl iodide and 0.45 mol of methyl acetate into a 500ml titanium reactor, first use argon to discharge the air in the reactor and pressurize to 2....

Embodiment 2

[0035] Preparation of carbonylation catalyst: Co(OAc) containing 8.98gCo, containing 2.75gLa and containing 3.25gSr 2 4H 2 O, La(OAc) 3 ·5H 2 O and Sr(OAc) 2 0.5H 2 O is fully mixed and dissolved in pure water to obtain 400ml of impregnation solution, and the specific surface of 1.0L is 165m 2 / g, spherical SiO with a pore volume of 0.98 and a diameter of 5.6 mm 2 The carrier was immersed in the above impregnating solution, left to stand for 2 hours and dried at 100° C. to obtain the catalyst. The carbonylation catalyst was analyzed by ICP, and the Co content was 8.98g / L, the La content was 2.75g / L, and the Sr content was 3.25g / L.

[0036] Synthesis of vinyl acetate:

[0037] Step (1): Add 1.5 mol of acetic acid, 0.05 mol of carbonylation catalyst, 0.10 mol of methyl iodide and 0.45 mol of methyl acetate into a 500ml titanium reactor, first use argon to discharge the air in the reactor and pressurize to 2.0MPa, then Inject carbon monoxide and hydrogen until the pressur...

Embodiment 3

[0051] Preparation of carbonylation catalyst: Co containing 7.00gCo, 1.00gCe and 1.00gZn 2 (CO) 8 、Ce(OAc) 3 ·6H 2 O and Zn(OAc) 2 2H 2 O is fully mixed and dissolved in acetic acid with a concentration of 10wt%, to obtain 400ml of impregnation solution, and the specific surface of 1.0L is 150m 2 / g, spherical Al with a pore volume of 0.90 and a diameter of 5.6mm 2 o 3 The carrier was immersed in the above impregnating solution, left to stand for 2 hours and dried at 80° C. to obtain the catalyst. The carbonylation catalyst was analyzed by ICP, and the Co content was 7.00 g / L, the Ce content was 1.00 g / L, and the Zn content was 1.00 g / L.

[0052] Synthesis of vinyl acetate:

[0053] Step (1): Add 1.5 mol of acetic acid, 0.05 mol of carbonylation catalyst, 0.10 mol of methyl iodide and 0.45 mol of methyl acetate into a 500ml titanium reactor, first use argon to discharge the air in the reactor and pressurize to 2.0MPa, then Inject carbon monoxide and hydrogen until the...

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Abstract

The invention relates to a method for preparing vinyl acetate to mainly solve the problems of low yield and low selectivity of vinyl acetate in the process of preparing vinyl acetate according to a route of carrying out carbonylation on methyl acetate at first and then carrying out cracking. By adoption of the technical scheme that the method for preparing vinyl acetate comprises the following steps: carrying out carbonylation on methyl acetate to obtain ethylidene diacetate, and carrying out cracking on ethylidene diacetate to obtain vinyl acetate, wherein a carbonylation catalyst adopts SiO2, Al2O3 or a mixture thereof as a carrier, and the active components comprise at least one of iron series elements, a lanthanide and at least one metal element selected from IIB and alkaline earth metals, the technical problems are well solved, and the method can be used for industrial production of vinyl acetate.

Description

technical field [0001] The present invention relates to a process for the preparation of vinyl acetate. Background technique [0002] Vinyl acetate (vinylacetate, VAC or VAM for short), is a colorless, transparent, flammable liquid at room temperature with a sweet ether fragrance. It is one of the most productive organic chemical raw materials in the world, widely used in the production of polyvinyl acetate (PVAc), polyvinyl alcohol, coatings, pastes, adhesives, vinylon, films, vinyl copolymer resins, acetal resins A series of chemical and chemical fiber products are widely used in various industries. [0003] The production of vinyl acetate adopts ethylene gas-phase method and acetylene gas-phase method both at home and abroad, which belong to the petrochemical process route. Since the rise of C1 chemistry, in the 1980s, the American Halcon (Halcon) company and the British Petroleum (BP) company successively A new process for the production of vinyl acetate from methanol ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C69/15C07C67/297B01J23/83
Inventor 查晓钟杨运信
Owner CHINA PETROLEUM & CHEM CORP