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co vapor phase synthesis of oxalate

A gas-phase synthesis and oxalate ester technology, which is applied in the direction of chemical instruments and methods, heterogeneous catalyst chemical elements, carbon monoxide or formate reaction preparation, etc., can solve the problems of low utilization rate of precious metals, high cost of catalysts, high content of precious metals in catalysts, etc. problems, to achieve the effects of shortened residence time, high combustion activity, and high effective utilization

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

[0014] The technical problem to be solved by the present invention is the high catalyst precious metal content in the prior art, the catalyst cost is high, the problem of precious metal utilization rate is low, a kind of method of new CO gas phase synthesis oxalate is provided

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] Take 60g from Al 2 o 3 For the coating and the cordierite honeycomb ceramic as the carrier of the inert core, the thickness of the coating is 80 μm. Take 0.03g of palladium chloride and 0.56g of lanthanum nitrate to prepare a 30ml solution as impregnation solution Ⅰ. Slowly add the impregnating solution I into the carrier, and turn the carrier to make the solution impregnate evenly, so as to prepare the catalyst precursor. The catalyst precursor was aged in the air for 20 hours, dried at 80°C, and then roasted in a muffle furnace at 450°C. After roasting, a carbon monoxide gas-phase synthesis oxalate catalyst was obtained. The catalyst composition was tested to be 0.03%Pd+0.3%La +80μm thick Al 2 o 3 The coating and cordierite honeycomb ceramics are the carrier of the inert core, and the distribution depth of Pd and La is 80 μm.

[0039] Get 40g and make catalyst and pack in reaction tube, feed hydrogen at volume space velocity and be 500 hours -1 , the temperature...

Embodiment 2

[0041] According to the preparation method of [Example 1], except that the catalyst composition is 0.01%Pd+1%Ce+150μm thick TiO 2 The coating and cordierite honeycomb ceramics are the carrier of the inert core, and the distribution depth of Pd and Ce is 150 μm.

[0042] Take 40 g of the prepared catalyst and put it into a reaction tube, feed hydrogen gas at a volume space velocity of 500 h −1 , and program the temperature to 200° C. for reduction for 6 hours. Then at a reaction temperature of 130°C, a reaction pressure of 0.2 MPa, a molar ratio of CO to methyl nitrite of 1.5, and a volumetric space velocity of 3000 h -1 Under the conditions of carbon monoxide gas phase synthesis of oxalate, the space-time yield of oxalate is 746g / L.cat.H, and the catalyst stability is 7000 hours.

Embodiment 3

[0044] According to the preparation method of [Example 1], except that the catalyst composition is 0.05%Pd+1%Sm+150μm thick SiO 2 The coating and cordierite honeycomb ceramics are the carrier of the inert core, and the distribution depth of Pd and Sm is 40 μm.

[0045] Take 40 g of the prepared catalyst and put it into a reaction tube, feed hydrogen gas at a volume space velocity of 500 h −1 , and program the temperature to 200° C. for reduction for 6 hours. Then, at a reaction temperature of 120°C, a reaction pressure of 0.5 MPa, a molar ratio of CO to methyl nitrite of 1.5, and a volumetric space velocity of 1000 h -1 Under the conditions of carbon monoxide gas phase synthesis of oxalate, the space-time yield of oxalate is 720g / L.cat.H, and the catalyst stability is 9500 hours.

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Abstract

The invention relates to a method of CO gas phase synthesis of oxalate and mainly solves the problems of high content of noble metals, high catalyst cost, low utilization rate of the noble metals of catalysts in the prior art. A technical scheme is characterized in that a layered composite carrier comprises a core selecting from at least one inert carrier of iolite honeycomb ceramic, metals, metal, quartz, spinel and mullite, and at least one coating combined to the core, selected from Al2O3, SiO2 and TiO2; and metallic palladium or a palladium oxide and rare earth element or rare earth element oxide catalysts are distributed in the coating of the layered composite carrier. The technical scheme well solves the problems, and the method can be used in the industrial production for the carbon monoxide gas phase synthesis of oxalate.

Description

technical field [0001] The invention relates to a method for synthesizing oxalate in CO gas phase. Background technique [0002] Oxalate is an important organic chemical raw material, which is widely used in fine chemical industry to prepare various dyes, medicines, solvents, extractants and various intermediates. In addition, hydrogenation of oxalate can produce ethylene glycol, a very important chemical raw material, and this route can replace the current method of producing ethylene glycol by the petroleum route with high cost. [0003] Traditional oxalate production routes include starch nitric acid oxidation method, cellulose alkali fusion method, sodium formate method, ethylene glycol one-step oxidation method, propylene oxidation method and oxalate alcohol esterification reaction method, but the above-mentioned traditional processes have high cost and energy consumption. Large, serious pollution, unreasonable use of raw materials and other shortcomings. Therefore, a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C69/36C07C67/36B01J23/63
CPCB01J23/002B01J23/63B01J2523/00C07C67/36C07C69/36B01J2523/31B01J2523/3706B01J2523/824B01J2523/3712B01J2523/47B01J2523/3737B01J2523/41
Inventor 龚海燕刘俊涛刘国强
Owner CHINA PETROLEUM & CHEM CORP