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Method for producing carbonate esters, and catalytic structure for producing carbonate esters

A manufacturing method and carbonate technology, which are used in catalyst activation/preparation, physical/chemical process catalysts, carbon dioxide or inorganic carbonate preparation, etc., can solve the problems of easy pulverization of cerium oxide powder, achieve excellent efficiency, inhibit powder effect of disintegration and disengagement

Pending Publication Date: 2021-02-26
NIPPON STEEL CORP +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0015] However, as a result of research conducted by the inventors of the present invention, a problem that cerium oxide powder is easily pulverized during the reaction has been encountered

Method used

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  • Method for producing carbonate esters, and catalytic structure for producing carbonate esters
  • Method for producing carbonate esters, and catalytic structure for producing carbonate esters
  • Method for producing carbonate esters, and catalytic structure for producing carbonate esters

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0155] 1. Manufacture of catalyst structure

[0156] Cerium oxide (manufactured by Solvay Special Chem Japan, HSA-20SP, average particle diameter of about 10 μm, impurity concentration of 0.02% or less) was fired at 873 K in an air atmosphere for 3 hours to obtain a powdery solid catalyst. Specifically, 20 g of cerium oxide was placed in a crucible in a muffle furnace (FO310 manufactured by Yamato Scientific Co., Ltd.), and then fired at a temperature increase rate of 10° C. / min to 873 K. The solid catalyst obtained in this way, a silica binder (manufactured by Asahi Chemical Industry Co., Ltd., SUMICERAM, P-750 (mainly a mixture of a siloxane-based binder and water)) and water were adjusted to a weight ratio of 2.05: Weigh in a 1:1 manner, prepare 50 g of the mixed solution for catalyst layer preparation, and fill a 50 cc beaker.

[0157] In addition, in order to prepare the intermediate layer between the catalyst layer and the catalyst-coated substrate, a 50 cc beaker was f...

Embodiment 2~4

[0175] By repeatedly dipping the metal honeycomb in the coating solution containing the cerium oxide powder, about 30 g / m of cerium oxide is adhered. 2 , 70g / m 2 , 150g / m 2 , except for this, in the same manner as in Example 1, the catalyst structures of Examples 2 to 4 were produced. The thicknesses of the catalyst layers of the structures obtained in this manner were estimated to be about 20 μm, about 50 μm, and about 100 μm, respectively.

[0176] As a result of reaction evaluation using each catalyst structure, the adhesion of Example 2 was 30 g / m 2 In the catalyst structure of , the DPrC yield reached a high yield of 57 mol%, while the by-product / DPrC was suppressed to 1.2 mol%. In addition, the adhesion of Example 3 was 70 g / m 2 In the catalyst structure of , the DPrC yield reached a high yield of 52 mol%, while the by-product / DPrC was suppressed at 1.4 mol%. In addition, the adhesion of Example 4 was 150 g / m 2 In the catalyst structure of , the DPrC yield reached ...

Embodiment 5

[0178] The same cerium oxide powder and silica binder (Asahi Chemical Industry Co., Ltd., SUMICERAM, P-700-D (mainly silica powder with an average particle size of about 5 μm, siloxane-based binder) as in Example 1 were used. A mixture of catalyst and water)) and water were weighed in a weight ratio of 2:0.95:1.5 to prepare 50 g of the mixed solution for catalyst layer preparation, filling a 50 cc beaker. Except for this, it was carried out in the same manner as in Example 2, and the adhesion 30 g / m of Example 5 was produced. 2 catalyst structure. The thickness of the catalyst layer at this time is estimated to be about 20 μm. As a result of the reaction evaluation using this structure, the yield of DPrC was as high as 54 mol%, and the by-product / DPrC was suppressed to 0.9 mol%. In addition, the cerium oxide powder did not peel off from the base material even after the reaction, and had high adhesiveness.

[0179] It was also confirmed that when each of the structures was s...

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Abstract

Provided are a method for producing carbonate esters, and a catalytic structure for producing carbonate esters, whereby the solid catalyst powder formation and detachment are suppressed, and superiorcarbonate ester reaction efficiency is yielded when a catalytic structure constituted by a sufficient quantity of a cerium-oxide-containing solid catalyst supported on a substrate is used. The methodfor producing carbonate esters according to the present invention comprises a step for reacting a monohydric alcohol and carbon dioxide in the presence of a catalytic structure and a hydrating agent.The catalytic structure comprises a substrate and a catalytic layer that is formed on at least a portion of the surface of the substrate and contains a solid catalyst and an inorganic binder. The solid catalyst contains cerium oxide. The supported quantity of the solid catalyst is 15 g / m2 to 200 g / m2, inclusive. The inorganic binder contains silica and / or alumina.

Description

technical field [0001] The present invention relates to a method for producing carbonate and a catalyst structure for producing carbonate. Background technique [0002] In recent years, attention to global warming has increased. In the COP (Conference of the Parties), an international framework for agreeing to reduce emissions of greenhouse gases, etc., as a long-term global common goal, the average temperature increase from before the Industrial Revolution to be kept below 2°C sufficiently low. We aim to suppress emission peaks as early as possible, and to reduce them drastically based on the latest technology. In the COP21 Paris Agreement, it is stipulated that all countries should commit themselves to formulate and propose a long-term low-emission development strategy for greenhouse gases. Among man-made greenhouse gases, carbon dioxide is considered to have the greatest influence, and various regions are working on developing countermeasures for carbon dioxide reductio...

Claims

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Application Information

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IPC IPC(8): C07C69/96C07B61/00B01J35/04C07C68/04B01J23/10
CPCC07C68/04B01J23/10Y02P20/141B01J37/0225B01J37/0215B01J35/56C07C69/96C07B61/00B01J21/08
Inventor 铃木公仁新开洋介刘红玉原田英文加藤让森田健太郎大桥亚珠香
Owner NIPPON STEEL CORP