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Diethylene acetate catalyst

A technology of diethylene acetate and catalysts, applied in the direction of physical/chemical process catalysts, organic chemistry, chemical instruments and methods, etc., can solve the problem of low selectivity, low yield of diacetate, and diacetate High selectivity issues, to achieve the effect of improving yield and selectivity, improving activity and stability

Active Publication Date: 2018-05-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] One of the technical problems to be solved by this invention is the problem of low yield of ethylene diacetate and low selectivity, and a new catalyst for ethylene diacetate is provided, which has the advantages of high yield of ethylene diacetate. The characteristics of high selectivity of diethylene acetate

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0027] Preparation of Catalyst Carrier II: Fully mix aluminum hydroxide powder containing 3.40g of Al with 10.0g of silica sol with a concentration of 35wt% to obtain a coating solution, and spray the coating solution evenly on 1.0L of spherical SiO with a diameter of 5.6mm 2 placed on the carrier for 1 hour under ventilated conditions, dried at 100° C., and then calcined at 450° C. for 4 hours to obtain the catalyst carrier precursor I. Zirconium oxychloride (ZrOCl) containing 0.6g Zr 2 ·8H 2 O) 0.6 L of aqueous solution was impregnated on 1.0 L of catalyst carrier precursor I, and dried at 100° C. to obtain the catalyst carrier II.

[0028] Preparation of main catalyst: RhCl containing 7.20gRh 3 ·3H 2 O was dissolved in pure water to obtain 580ml of impregnating solution, and 1.0L of the catalyst carrier II was impregnated in the above impregnating solution, left to stand for 3h and dried at 100°C, and 2 The main catalyst was obtained by raising the temperature to 500° C...

Embodiment 2

[0070] Preparation of Catalyst Carrier II: Fully mix pseudo-boehmite powder containing 3.40g Al with 10.0g of silica sol with a concentration of 35wt% to obtain a coating solution, and spray the coating solution evenly on a 1.0L spherical surface with a diameter of 5.6mm SiO 2 placed on the carrier for 1 hour under ventilated conditions, dried at 100° C., and then calcined at 450° C. for 4 hours to obtain the catalyst carrier precursor I. Zirconium oxychloride (ZrOCl) containing 0.60g Zr 2 ·8H 2 O) 0.6 L of aqueous solution was impregnated on 1.0 L of catalyst carrier precursor I, and dried at 100° C. to obtain the catalyst carrier II.

[0071] Preparation of main catalyst: RhCl containing 7.20gRh 3 ·3H 2 O was dissolved in pure water to obtain 580ml of impregnating solution, and 1.0L of the catalyst carrier II was impregnated in the above impregnating solution, left to stand for 3h and dried at 100°C, and 2 The main catalyst was obtained by raising the temperature to 500...

Embodiment 3

[0076] Preparation of Catalyst Carrier II: Fully mix boehmite powder containing 3.40g Al with 10.0g silica sol with a concentration of 35wt% to obtain a coating solution, and spray the coating solution evenly on 1.0L of spherical SiO with a diameter of 5.6mm 2 placed on the carrier for 1 hour under ventilated conditions, dried at 100° C., and then calcined at 450° C. for 4 hours to obtain the catalyst carrier precursor I. Zirconium oxychloride (ZrOCl) containing 0.60g Zr 2 ·8H 2 O) 0.6 L of aqueous solution was impregnated on 1.0 L of catalyst carrier precursor I, and dried at 100° C. to obtain the catalyst carrier II.

[0077] Preparation of main catalyst: RhCl containing 7.20gRh 3 ·3H 2 O was dissolved in pure water to obtain 580ml of impregnating solution, and 1.0L of the catalyst carrier II was impregnated in the above impregnating solution, left to stand for 3h and dried at 100°C, and 2 The main catalyst was obtained by raising the temperature to 500° C. and calcining...

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Abstract

The invention relates to a diethylene acetate catalyst, which mainly solves the problem of low activity and selectivity of the diacetate catalyst in the prior art. By adopting a diacetate catalyst, the catalyst includes a main catalyst and a cocatalyst, and the main catalyst includes a carrier and an active component; the active component adopts a compound of rhodium; the cocatalyst is an iodide; The carrier is silicon dioxide with an aluminum coating on its surface and modified with a modified metal element; the content of the aluminum is 1.00-10.00g / L; the content of the modified metal element is 0.010-1.00g / L; the modified The technical proposal that the metal element is selected from at least one of IVB metal elements solves this problem well and can be used in the industrial production of vinyl acetate.

Description

technical field [0001] The present invention relates to diethylene acetate catalyst, preparation method and application. Background technique [0002] Vinyl acetate (VAc) is one of the 50 largest chemical raw materials in the world. Polyvinyl alcohol (PVA), polyvinyl acetate (PVAc) emulsion, and vinyl acetate-ethylene copolymer emulsion can be produced by self-polymerization or copolymerization with other monomers. (VAE) or copolymer resin (EVA), vinyl acetate-vinyl chloride copolymer (EVC) and other derivatives. These derivatives are widely used in adhesives, architectural coatings, sizing agents for paper or fabrics, coatings, inks, leather processing, fiber processing, emulsifiers, water-soluble films, and soil conditioners. [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 (Halc...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/13C07C67/36C07C69/16
Inventor 查晓钟杨运信张丽斌
Owner CHINA PETROLEUM & CHEM CORP