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Method for preparing isosorbide

A technology of isosorbide and sorbitol, applied in the field of preparation of isosorbide, can solve the problems of high production cost, low catalytic activity, increased production cost and the like, and achieves the effects of low corrosiveness, good catalytic performance and cost saving

Active Publication Date: 2019-08-06
CHENGDU ORGANIC CHEM CO LTD CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In 2009, Huang He et al. (CN101691376A) used immobilized heteropolyacid as a catalyst to prepare isosorbide, but it was difficult to solve the problem that the heteropolyacid was easily lost in aqueous solution, and the reaction temperature as high as 250°C greatly increased the production cost
[0004] However, in the above studies, SO 4 2- The / MxOy-type solid acid has low catalytic activity for the preparation of isosorbide from sorbitol dehydration. In order to achieve a higher yield of isosorbide, a high temperature close to 200 ° C is required, and the production cost is relatively high.

Method used

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  • Method for preparing isosorbide

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preparation example Construction

[0027] A preparation method of isosorbide, comprising the steps of:

[0028] [1] heating and melting solid sorbitol in a reactor to obtain a melt;

[0029] [2] Add SO to the melt obtained in step [1] 4 2- / ZrO 2 -Al 2 o 3 Immobilized acid catalyst;

[0030] [3] After step [2], the reactor is heated and depressurized, and the sorbitol in the melt undergoes a dehydration reaction to obtain isosorbide.

[0031] preferred, SO 4 2- / ZrO 2 -Al 2 o 3 The immobilized acid is prepared by co-precipitation method, sol-gel method or solvent-free grinding method.

[0032] Further preferably, the co-precipitation method includes the following steps: dissolving a certain amount of aluminum salt and zirconium salt in deionized water, adding 20%-28% ammonia water dropwise during the stirring process until the pH value of the system reaches 9-11 and co-precipitation occurs, Then filter the solution, dry the obtained precipitate at 100-120°C for 24h, soak the dried precipitate in an ...

Embodiment 1

[0039] The catalyst of this embodiment adopts co-precipitation method to prepare SO 4 2- / ZrO 2 -Al 2 o 3 catalyst. 0.103g of Al 2 (SO 4 ) 3 and 3.22 g of ZrOCl 2 ·8H 2 O was dissolved in 50ml deionized water, and 25%-28% ammonia water was added dropwise during the stirring process until the pH value of the system was 9-11, and co-precipitation occurred. The filtered sample was dried at 110°C for 24 hours, and the dried sample was soaked in an appropriate amount of 0.5 M in sulfuric acid solution, centrifuged after 5h, dried at 110°C for 24h, and calcined at 550°C in air for 5h to obtain SO with an Al / Zr molar ratio of 0.06 4 2- / ZrO 2 -Al 2 o 3 .

Embodiment 2

[0041] The catalyst of this embodiment adopts sol-gel method to prepare SO 4 2- / ZrO 2 -Al 2 o 3 catalyst. Add 20.2g of 37% hydrochloric acid to 100g of deionized water, add 5.99g of zirconium n-propoxide (70% n-butanol solution) and 0.157g of aluminum isopropoxide to the solution under stirring, and continue stirring After 5 hours, transfer to a polytetrafluoroethylene-lined hydrothermal kettle, place at 100°C for 24 hours, filter and wash to obtain a white precipitate, immerse 1g of the dried white precipitate in 15ml of 0.5M ammonium bisulfate solution, Centrifuge after 5 hours, dry at 120°C, and then calcinate at 550°C in air for 5 hours to obtain SO with an Al / Zr molar ratio of 0.06. 4 2- / ZrO 2 -Al 2 o 3 .

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Abstract

The invention belongs to the technical field of supported acid catalysis, and concretely relates to a method for preparing isosorbide. The method is used for solving the problem of poor catalytic activity of existing SO<4><2-> / MxOy supported acids for dehydrating sorbitol to prepare isosorbide and the problem of high production cost due to a high temperature approaching 200 DEG C, needed by reaching a high isosorbide yield. The method in the invention is characterized in that sorbitol used as a reaction raw material is continuously dehydrated under heating and low-vacuum reaction conditions with a supported acid SO<4><2-> / ZrO2-Al2O3 as a catalyst to prepare isosorbide; and the SO<4><2-> / ZrO2-Al2O3 supported acid can be prepared by a coprecipitation process, a sol-gel process or a solventless grinding process. The method is suitable for dehydration of sorbitol to prepare isosorbide.

Description

technical field [0001] The invention belongs to the technical field of solid-supported acid catalysis, and in particular relates to a preparation method of isosorbide. Background technique [0002] Isosorbide is the dehydration product of sorbitol, which can be widely used in food, medicine, polymer plastics and other fields. The current research hotspot is to use isosorbide as a polymerization monomer in the field of polymer production. If it is added to polyethylene terephthalate (PET), it can increase the glass transition temperature of the polymer and increase the strength of the polymer. Wait. Therefore, the preparation of isosorbide by dehydration of biomass-derived product sorbitol has great research value and industrial application prospect. However, in industry, liquid acids such as sulfuric acid are usually used as catalysts for the dehydration of sorbitol to prepare isosorbide, which has disadvantages such as corrosion of equipment, pollution of the environment,...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07D493/04B01J27/053
CPCB01J23/002B01J27/053C07D493/04
Inventor 陈彤张怡王公应张华
Owner CHENGDU ORGANIC CHEM CO LTD CHINESE ACAD OF SCI