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Glycol as catalyst prepared by hydrogenising oxalate as well as forming method and application thereof

A molding method and catalyst technology, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., can solve the problem of low yield of finished products, low space velocity, and high wear rate problem, to achieve the effect of good activity and selectivity, long service life and high mechanical strength

Active Publication Date: 2013-01-09
SHANGHAI HUAYI ENERGY CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Patents related to oxalate hydrogenation synthesis of ethylene glycol catalysts have been reported, and the main scope of the invention revolves around copper-silicon catalysts (EP 46983 A1, Zhao 57-122939, JP 06135895 A2, US4649226, etc.), but the reaction hydrogen ester is relatively high , the liquid hourly space velocity is low, and multi-carbon alcohol by-products will be produced during the hydrogenation of oxalate ester to ethylene glycol, which is difficult to separate and consumes a lot of energy
The molding involved is mainly tablet pressing method and traditional dry powder extrusion method. The prepared catalyst has low strength and high wear rate. After the catalyst raw powder is formed, the finished product yield is low and the unit consumption is high. The active components cause catalyst activity, selectivity and life to decrease, and a large amount of toxic and harmful dust that is inevitably generated during the molding process pollutes the environment

Method used

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  • Glycol as catalyst prepared by hydrogenising oxalate as well as forming method and application thereof
  • Glycol as catalyst prepared by hydrogenising oxalate as well as forming method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] One with 40CuOx / SiO 2 (wherein, x is 1 / 2 of Cu valence number,) the preparation and molding method of the copper silicon oxalate hydrogenation catalyst represented are as follows:

[0020] Pour 45g of treated white carbon black into a round-bottomed flask, mix with 100g of deionized water and add acid to adjust the pH to 3 to obtain solution A. Solution A was added to the solution containing 118g Cu(NO 3 ) 2 copper nitrate solution, and adjust the pH of the mixture to 8 with 5% ammonia water, and heat up to 75°C for aging for 22 hours. After the reaction was completed, the feed liquid was filtered while it was hot, washed with deionized water several times, washed with ethanol and suction filtered to a certain amount of retained water, and then uniformly dehydrated at 95°C so that the retained water rate in the material was 52wt%. The material is kneaded to obtain a solid wet material. The solid wet material is molded into a strip with a diameter of 5.9mm under a pr...

Embodiment 2~4

[0024] In addition to changing the water retention rate in the dehydration process, all the other catalysts were prepared under the same conditions and methods as in Example 1. The mechanical strength of the molded catalyst and the results after 8 hours of hydrogenation of oxalate were listed in Table 1.

[0025] Table 1 The strength, attrition rate and 8-hour results of oxalate hydrogenation reaction of shaped catalysts at different water retention rates

[0026] name Example 1 Example 2 Example 3 Example 4 Water retention rate, % mass 52 85 70 15 Longitudinal strength, N / cm 2 958.3 723.5 850.3 910.3

[0027] Transverse strength, N / cm 190.1 204.9 195.1 173.2 Wear rate, % 0.594 0.793 0.802 1.623 Oxalate conversion rate, % 99.2 98.3 99.1 98.9 Ethylene glycol selectivity, % 92.6 93.6 94.3 93.5 name Comparative example 1 Comparative example 2

Embodiment 5~7

[0033] Except changing dehydration temperature, all the other are prepared catalyst by the same condition and method of embodiment 1, the mechanical strength of the catalyst after molding and the result after reacting for 8 hours are listed in table 2

[0034] The strength of shaped catalyst under table 2 different dehydration temperatures, the attrition rate and the result of 8 hours of reaction

[0035] name Example 1 Example 5 Example 6 Example 7 Dehydration temperature, ℃ 95 80 110 120 Longitudinal strength, N / cm 2 958.3 897.3 698.3 496.1 Transverse strength, N / cm 190.1 132.1 100.1 78.3 Wear rate, % 0.594 0.789 4.035 10.013 Oxalate conversion rate, % 99.2 99.1 99.6 99.3 Ethylene glycol selectivity, % 92.6 93.5 92.1 91.9

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Abstract

The invention discloses a glycol as a catalyst prepared by hydrogenising oxalate as well as a forming method and application thereof. The forming method comprises the following steps of: preparing a feed liquid containing catalyst raw powder; then filtering, washing, leaching, drying and dehydrating the feed liquid during heating until the water weight content of a filter cake is 15-85 percent; kneading, extruding, forming, gelatinizing and exposing in the air for ageing; and drying and heating the aged product in the nitrogen atmosphere of 250-450 DEG C to obtain a finished product of the catalyst, wherein the catalyst is a copper-silicon system, a copper-silicon oxide system, a copper-alumina system, a copper-titanium oxide system, a copper-zinc oxide system, a copper-chromic oxide system and a copper-zirconium oxide system. The catalyst prepared by the method has a certain shape and size as well as the advantages of high mechanical strength, low abrasion rate, no dust generation inthe forming process, economy, environmental protection, long service life and favorable activity and selection in the reaction process of synthesizing the glycol prepared by hydrogenising the oxalate.

Description

technical field [0001] The invention relates to a catalyst for synthesizing ethylene glycol by the hydrogenation reaction of oxalic acid ester. Background technique [0002] Ethylene glycol is an important raw material for organic synthesis. There are more than a hundred kinds of chemical products derived from ethylene glycol, which are widely used in synthetic fibers, plastics, coatings, military industry, construction and other fields. [0003] At present, most of the ethylene glycol in the world uses ethylene oxide (EO) direct hydration method, also known as the process route of pressurized hydration method, but this method has insurmountable shortcomings, mainly in the long process flow and water ratio (H2O and The molar ratio of EO) is high, the energy consumption is large, and the selectivity of ethylene glycol is relatively low. In the 1980s, Japan's Ube Industries and United Carbide jointly developed a process that uses dimethyl oxalate as a raw material to hydrogen...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C29/12B01J35/02B01J23/80B01J23/86C07C31/20B01J35/00
Inventor 王东辉李永刚吴良泉周亚明戴成勇唐大川施春晖肖本端
Owner SHANGHAI HUAYI ENERGY CHEM