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Method for producing carbonate compound

A manufacturing method and compound technology, applied in the new manufacturing field of carbonate compounds, can solve the problems that various carbonate compounds cannot be manufactured separately, hydrogen chloride corrodes manufacturing equipment, phosgene is toxic, etc.

Inactive Publication Date: 2010-11-10
ASAHI GLASS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] However, the method (1) has the problem that only cyclic carbonates can be produced, and various carbonate compounds cannot be produced separately.
[0008] (2) There are problems such as by-product hydrogen chloride corrodes manufacturing equipment, phosgene has toxicity in the method of (2)
[0009] The method of (3) is an equilibrium reaction, so there are problems such as the need to use a large excess of alcohol in order to increase the yield of the target product, and the asymmetric carbonate compound as a by-product is difficult to separate and remove.
[0010] The method of (4) has problems such as by product hydrogen chloride corrosion manufacturing equipment
[0018] In the examples of (7), (8), it is reported that in the presence of a catalyst, chloroform and cyclic carbonate compounds are generated through the reaction of hexachloroacetone and alcohol, but, according to the inventor's research, the ortho position is adjacent to the hydroxyl group Diol compounds, the reaction rate of the reaction to form carbonate by intramolecular cyclization is very fast, and it is expected that it is difficult to be directly applied to the reaction of other diols or monohydric alcohols

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment

[0219] Hereinafter, the present invention will be described more specifically with reference to examples, but the present invention is not limited to these examples.

[0220] Examples 1 to 16 are examples, and examples 17 and 18 are comparative examples.

[0221] (Gas chromatography)

[0222] Gas chromatography (hereinafter referred to as GC) analysis was performed using 6890 series manufactured by Agilent.

[0223] (molecular weight)

[0224] The measurement of the number average molecular weight (hereinafter referred to as Mn) and the weight average molecular weight (hereinafter referred to as Mw) was performed using gel permeation chromatography (manufactured by Tosoh Corporation, HLC-8220 GPC) (hereinafter referred to as GPC). Mn and Mw are molecular weights based on polystyrene.

example 1

[0226] In a 500 mL glass reactor with a stirrer, a reflux condenser at 20°C and a distillation line, add 262 g (0.99 mol) of hexachloroacetone, 150 g (1.97 mol) of 1,2-propanediol and 4 g of tetrabutylammonium bromide (hereinafter referred to as TBAB), the temperature was gradually raised while stirring, and the reaction was performed at an internal temperature of 120°C. The reaction was performed for 10 hours while distilling off chloroform generated by the reaction from a distillation line. After completion of the reaction, the fraction distilled off from the distillation line and the crude reaction liquid present in the reactor were collected to obtain 407.8 g of the recovered crude liquid (recovery rate: 98%). The organic components recovered by simple distillation of the recovered crude liquid under vacuum were analyzed by GC. As a result, it was confirmed that the compounds shown in Table 1 were produced in the yields shown in Table 1.

[0227] As can be seen from the r...

example 2

[0231] The reaction was carried out in the same manner as in Example 1 except that the amount of 1,2-propanediol was changed to 75 g (0.99 mol). After completion of the reaction, the distilled fraction from the distillation line and the crude reaction liquid present in the reactor were recovered to obtain 328.6 g of the recovered crude liquid (recovery rate: 96.36%). The organic components recovered by simple distillation of the recovered crude liquid under vacuum were analyzed by GC. As a result, it was confirmed that the compounds shown in Table 2 were produced in the yields shown in Table 2.

[0232] As can be seen from the results in Table 2, the conversion rate of hexachloroacetone is 100%, the yield of 1,2-propylene carbonate based on hexachloroacetone is 94%, and the yield of chloroform is 95%.

[0233] Table 2

[0234] compound

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Abstract

Disclosed is a novel method by which various carbonate compounds can be freely produced with high yield without using phosgene and without by-producing hydrogen chloride. Specifically disclosed is a method wherein a compound having a carbonate bond is obtained by reacting a compound (1) shown below with a compound having one OH group or a compound having two or more OH groups in the presence of a halogen salt. In the formula (1) below, X1-X6 respectively represent a hydrogen atom or a halogen atom; at least one of X1-X3 represents a halogen atom; and at least one of X4-X6 represents a halogen atom.

Description

technical field [0001] The present invention relates to a novel production method of carbonate compounds. Background technique [0002] The following methods are known as methods for producing carbonate compounds. [0003] (1) A method of producing a cyclic carbonate by reacting carbon dioxide and alkylene oxide in the presence of a catalyst (for example, refer to Patent Document 1). [0004] (2) Make phosgene (COCl 2 ) reacts with alcohol to produce a dialkyl carbonate or a cyclic carbonate (for example, refer to Patent Document 2). [0005] (3) A method of producing by transesterification of a cyclic carbonate or dimethyl carbonate with an alcohol in the presence of a transesterification catalyst (for example, refer to Non-Patent Document 1). [0006] (4) A method of producing by reaction of methyl chloroformate and alcohol (for example, refer to Patent Document 2). [0007] However, the method (1) has a problem that only cyclic carbonates can be produced, and various ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C68/00C07C69/96C07D317/36C07D317/38C07D319/06C07B61/00
CPCC07D319/06C07D317/38C07D317/36C07C68/00C07C69/96
Inventor 冈本秀一田岛宏平冈添隆
Owner ASAHI GLASS CO LTD