Preparation method of solid acid catalyst used for biomass hydrolysis

A solid acid catalyst and biomass technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems that catalysts cannot be recycled, the demand for chemical reagents is large, and the cost of cellulase is high. Good catalytic effect, low price, high hydrolysis strength

Active Publication Date: 2013-05-22
GUANGZHOU INST OF ENERGY CONVERSION - CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although biomass hydrolysis and saccharification technology has achieved fruitful results, there are still some key problems to be solved, mainly reflected in: the loss of sugar during liquid acid catalyzed hydrolysis, and the catalyst cannot be recycled, and subsequent treatment of the reaction solution is required; The catalytic system composed of liquid has a large demand for chemical reagents, high cost, and the subsequent treatment process is relatively complicated; high-temperature liquid water does not need to add chemical reagents, but it requires high temperature and high pressure operation, which consumes a lot of energy, and requires the reaction device. High; although enzymatic hydrolysis has good orientation, the reaction cycle is long and the cost of cellulase is high

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Weigh 100g of pine wood chips, put them in an oven after cleaning, and dry them at a temperature of 105°C until they reach a constant weight; put the dried sawdust into a closed reactor, and react for 5 hours under nitrogen protection and a reaction temperature of 450°C , to obtain a black powder, cooled to room temperature; get 20g of black powder and 400ml of fuming sulfuric acid (SO 3 15wt%) was placed in a three-necked flask, reacted for 20h under the conditions of nitrogen protection, stirring and 80°C reaction temperature, until the reaction solution reached the maximum acidity constant value, cooled to room temperature, filtered to remove black solid powder, and used Wash with deionized water until no ions are detected, and then dry; take the dried black solid powder and place it in a three-necked flask, add a sufficient amount of CuCl 2 The solution was protected by nitrogen gas, and stirred in a water bath at 30°C for 20 hours. After the reaction was completed...

Embodiment 2

[0028] Weigh 100g of sweet sorghum stalks, put them in an oven after cleaning, and dry them at a temperature of 105°C to constant weight; put the dried sawdust into a closed reactor, and react under nitrogen protection and a reaction temperature of 400°C After 10 hours, a black powder was obtained and cooled to room temperature; 20 g of the black powder and 400 ml of concentrated sulfuric acid were placed in a three-necked flask, and reacted for 1 h under the conditions of nitrogen protection, stirring and a reaction temperature of 200 ° C, cooled to room temperature, and filtered to remove the black The solid powder is washed with deionized water until no ions are detected, and then dried; the dried black solid powder is placed in a three-necked flask, and a sufficient amount of K 2 SO 4 The solution was protected with nitrogen gas, and stirred in a water bath at 80°C for 5 hours. After the reaction was completed, it was suction filtered and washed with deionized water until ...

Embodiment 3

[0032] Weigh 100g of microcrystalline cellulose, put it in an oven after cleaning, and dry it at a temperature of 105°C until it reaches a constant weight; put the dried sawdust into a closed reactor, under the conditions of nitrogen protection and a reaction temperature of 600°C React 1h, obtain black powder, be cooled to room temperature; Get the oleum of 20g black powder and 400ml (SO 3 15wt%) was placed in a three-necked flask, reacted for 10 h under nitrogen protection, stirring and a reaction temperature of 90° C., cooled to room temperature, filtered to remove black solid powder, and washed with deionized water until no ions were detected. Then dry; take the dried black solid powder and place it in a three-necked flask, add a sufficient amount of Na 2 SO 4The solution was protected by nitrogen gas, and stirred in a water bath at 60°C for 1 hour. After the reaction was completed, it was suction-filtered and washed with deionized water until no ions were detected, and t...

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Abstract

The invention belongs to the field of catalyst preparation, relates to a solid acid catalyst, and in particular relates to a preparation method of a solid acid catalyst used for the production of fermentable sugars by hydrolyzing and saccharifying lignocellulose biomass. The preparation method of the solid acid catalyst comprises the following steps of: carbonizing raw materials or catalyst carriers, chemically modifying the materials, adding catalytically-active metal ions, and drying and grinding. The catalyst provided by the invention is easily obtained and low in price; the acidity is controllable and adjusted according to the needs of reaction; and compared with traditional liquid acid catalysts, the solid acid catalyst can be recycled and reused, has a low requirement for corrosion resistance of equipment, requires low reaction temperature and consumes less energy. The solid acid catalyst is widely applied and particularly applied to the hydrolysis and saccharification process of lignocellulose biomass, and can ensure that the hydrolysis and saccharification process becomes efficient, environment-friendly and energy-saving; and the solid acid catalyst has practical significance for promoting large-scale application of the hydrolysis and saccharification process.

Description

technical field [0001] The invention belongs to the field of catalyst preparation, and relates to a preparation method of a solid acid catalyst, in particular to a preparation method of a solid acid catalyst required for hydrolyzing lignocellulosic biomass to produce fermentable sugar. technical background [0002] The current world's energy supply mainly depends on fossil energy, and the non-renewability of fossil energy means that it will be exhausted one day. At the same time, the environmental pollution caused by automobile exhaust is becoming more and more serious. The "contribution rate" of automobile exhaust to air pollution indicators such as sulfur oxides and nitrogen oxides in Beijing, Shanghai and Guangzhou has reached more than 60%, and has become a major source of air pollution. . [0003] Fuel ethanol is not only the most direct and convenient substitute for petroleum-based liquid fuels, but also can effectively reduce carbon dioxide emissions, and has been ap...

Claims

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Application Information

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Patent Type & AuthorityPatents(China)
IPC IPC(8): B01J27/055B01J27/053B01J31/26B01J29/00C13K1/02C13K13/00
Inventor亓伟王琼袁振宏庄新姝许敬亮张宇谭雪松徐惠娟余强
OwnerGUANGZHOU INST OF ENERGY CONVERSION - CHINESE ACAD OF SCI