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Catalyst for synthesizing glycol from hydrogenation of methyl glycolate, and preparation method and application thereof

A technology of methyl glycolate and catalyst, which is applied to a catalyst for synthesizing ethylene glycol by hydrogenation of methyl glycolate, a preparation method and an application field, can solve the problems of long process flow and high cost of raw materials in the production process of oxalate, and achieve stable catalyst stability. Good performance, simple preparation method and low production cost

Active Publication Date: 2015-04-29
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Patents CN102247847A and CN102247868A disclose catalysts and applications for hydrogenation of oxalate esters to ethylene glycol, but the production process of oxalate esters is relatively long and the cost of raw materials is relatively high

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Weigh 6.20 g of copper nitrate and 2.7 g of nickel nitrate respectively, add the above salts into deionized water, and impregnate 16 g of zirconia in equal volume. The zirconia impregnated with the solution was placed at room temperature for 4 h, dried at 35 °C for 3 h, dried at 110 °C for 7 h, and calcined at 500 °C for 5 h. The obtained sample was subjected to a space velocity of 6000 h -1 , H at a pressure of 0.5 MPa 2 Under the atmosphere, the temperature was raised to 400 °C at a rate of 3 ml / min, and the temperature was maintained for 4 h. After the sample temperature dropped to room temperature, the O 2 0.5% O by volume 2 / N 2 at 1800h -1 Passivation at space velocity for 3 h. The obtained catalyst has a copper percentage of 9.0 wt%, a nickel percentage of 3.0 wt%, and a carrier zirconia of 88.0 wt%.

[0019] 2 ml of the above-mentioned catalyst was loaded into a fixed-bed tubular reactor. The catalyst was placed at a space velocity of 3500 h -1 , H at...

Embodiment 2

[0021] Weigh 11.52 g of copper nitrate and 0.83 g of manganese nitrate respectively, add the above salts into deionized water, and impregnate 12 g of silicon dioxide in equal volume. The silica impregnated with the solution was left at room temperature for 3 h, dried at 50 °C for 5 h, dried at 110 °C for 8 h, and calcined at 400 °C for 6 h. The obtained sample was subjected to a space velocity of 5000 h -1 , H at a pressure of 0.9 MPa 2 Under the atmosphere, the temperature was raised to 450 °C at a rate of 0.5 ml / min, and the temperature was maintained for 6 h. After the sample temperature dropped to room temperature, the O 2 1.0% O by volume 2 / N 2 at 1500h -1 Passivation at space velocity for 2 h. The obtained catalyst has a copper percentage of 20.0 wt%, a manganese percentage of 1.2 wt%, and a carrier silica of 78.8 wt%.

[0022] 2 ml of the above-mentioned catalyst was loaded into a fixed-bed tubular reactor. The catalyst was placed at a space velocity of 4000 ...

Embodiment 3

[0024] Weigh 10.80 g of copper nitrate and 0.94 g of cobalt nitrate respectively, add the above salts into deionized water, and impregnate 16 g of zirconia in equal volume. The zirconia impregnated with the solution was left at room temperature for 5 h, dried at 60 °C for 3 h, dried at 120 °C for 6 h, and calcined at 600 °C for 3 h. The obtained sample was subjected to a space velocity of 3500 h -1 , H at a pressure of 0.5 MPa 2 Under the atmosphere, the temperature was raised to 500 °C at a rate of 2 ml / min, and the temperature was maintained for 3 h. After the sample temperature dropped to room temperature, the O 2 1.5% O by volume 2 / N 2 at 2000h -1 Passivation at space velocity for 3 h. The obtained catalyst has a copper percentage of 15.0 wt%, a cobalt percentage of 1.0 wt%, and a carrier zirconia of 84.0 wt%.

[0025] 2 ml of the above-mentioned catalyst was loaded into a fixed-bed tubular reactor. The catalyst was placed at a space velocity of 3000 h -1 , H a...

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PUM

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Abstract

The invention relates to a catalyst for synthesizing glycol from hydrogenation of methyl glycolate, and a preparation method and an application thereof. The catalyst is mainly composed of a main metal Cu, an auxiliary metal which is one selected from Ni, Mn or Co, and a carrier, wherein the weight proportional composition of the catalyst is as follows: 9.0-20.0 wt% of Cu, 1.0-3.0 wt% of Ni, Mn or Co and 78.8-88.5 wt% of the carrier. The catalyst is simple in preparation method and low in production cost. The synthesized ethanol from hydrogenation of methyl glycolate is mild in reaction conditions, and has the advantages of high transformation rate of methyl glycolate, high selectivity of glycol and good catalyst stability.

Description

technical field [0001] The invention belongs to a catalyst for synthesizing ethylene glycol, a preparation method and application, in particular to a catalyst, a preparation method and an application for synthesizing ethylene glycol by hydrogenation of methyl glycolate. Background technique [0002] Ethylene glycol is an important raw material for the production of polyethylene terephthalate, lubricants, nonionic surfactants, and explosives. Ethylene glycol is also an important antifreeze agent in industries such as automobiles and aviation, and can also be used to produce special media and solvents. Since 2003, my country's ethylene glycol self-sufficiency rate has been below 30%, and my country's ethylene glycol is in a serious situation of short supply. [0003] At present, the production of ethylene glycol in the world mainly adopts petroleum routes, that is, ethylene and oxygen are used as raw materials, and ethylene is directly oxidized to ethylene oxide in the presen...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J23/889B01J23/75C07C31/20C07C29/149
Inventor 李德宝陈从标贾丽涛肖勇
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI