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Method for producing ethanol or acetone and butanol by taking lignocellulose as raw material

A technology for acetone and raw materials, which is applied in the field of producing ethanol or acetone butanol, can solve the problems of high investment cost, long enzymatic hydrolysis time and large area, and achieve the effects of low energy consumption and high hydrolysis efficiency

Active Publication Date: 2013-09-25
SHANDONG UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] Patent CN200810049574 (Publication No. CN101381743A) "Method for Producing Hydrogen and Ethanol from Straw Biomass Through Solid State Enzymolysis Pretreatment" analyzed the advantages and disadvantages of a series of such patents, while the CN200810049574 patent used grinding, enzymolysis, fermentation and other processes. Mix with a solid-liquid ratio of 1:1 and 1:8, and then add solid enzymes in a certain proportion. The enzymolysis time is 3 to 25 days. The enzymolysis time is long, and the enzymolysis efficiency is low, the production cycle is long, and the floor area is large. , unfavorable factors such as high investment costs

Method used

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  • Method for producing ethanol or acetone and butanol by taking lignocellulose as raw material
  • Method for producing ethanol or acetone and butanol by taking lignocellulose as raw material

Examples

Experimental program
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Effect test

Embodiment 1

[0036] The corncobs were crushed into 1mm powder with a pulverizer, washed with water, and then dried overnight at 60°C. Mix 500g of corncob powder below 1-2mm with 10L of water, and place it for anaerobic fermentation at 10°C for 1 day. When the pH drops to 4.5, adjust the wet disc grinder——Japan MKZA10 ultrafine particle melting machine (Mashiko Sangyo Co., Ltd., Japan) The gap between the two upper and lower disc grinding discs is 1 micron to the appropriate gap, mix the feed liquid refrigerated at 4°C, add it to the ultra-fine melting machine, grind for 10-15 laps, and the particle size is 2 μm Between, the soluble sugar content is 0.385g / g corn cob, wherein the glucose content is about 65%, and the xylose content is about 20%. Add the pretreatment solution to the compound cellulase in an amount of 5%. The hydrolysis conditions are: 10.0mL pH4.5, 50°C, 200rpm rotary shaking for 48h. The soluble sugar content is 0.637g / g corn cob, among which the xylose content can reach ...

Embodiment 2

[0038] Corn cobs were pulverized into 2mm powder with a pulverizer. Mix 500g of corncob powder below 2mm with 5L of water, place it at 4°C for 1 day, and place it for anaerobic fermentation at 4°C for 2 days, and when the pH drops to 5.0, adjust the wet disc grinder——Japan MKZA10 ultrafine particle fusion Crusher (Mashiko Sangyo Co., Ltd., Japan) the gap between the 2 upper and lower disc grinding discs to a suitable gap of 2 microns, after grinding for 15 circles, add 10FPU / g Acremonium composite cellulase and 0.4% β- Xylosidase; after mixing, pre-hydrolyze at 50°C for 1 hour, add 0.1% yeast powder, keep the temperature at 37°C after mixing, insert acetone-butanol-producing microorganism Clostridium beijerinckii ATCC55025 at an inoculum size of 5%, and ferment 72h, butanol content is 7.8g / L, acetone content is 4.1g / L.

Embodiment 3

[0040] Grind the bran into 1mm powder with a pulverizer, mix 500g of the feed liquid with 5L of water, and place it for anaerobic fermentation at 4°C for 2 days. When the pH drops to 4.8, adjust the wet disc grinder——Japan MKZA10 The gap between the two upper and lower discs of the particle melting machine (Mashiko Sangyo Co., Ltd., Japan) to a suitable gap of 10 microns, mix the anaerobic feed liquid at 4°C, add it to the ultra-fine melting machine, and grind for 10 laps , the soluble sugar content is 0.151g / g bran. Add 6.4 FPU / g Acremonium cellulase (compound enzyme with endoenzyme and exoenzyme) and 40 μL / g β-xylosidase to the pretreatment liquid at an additive amount of 5% for hydrolysis for 48 hours. The soluble sugar content is 0.531g / g bran. Add 0.1% of yeast powder to the mixed material liquid after pretreatment and enzymolysis of the above bran, and add 0.1% yeast powder, pH 5.5 to 7.0, insert acetone butanol production microorganism Clostridium beijerinckii ATCC5502...

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Abstract

The invention relates to a method for producing ethanol or acetone and butanol by taking lignocellulose as a raw material. According to the invention, a wet disc grinding machine-ultrafine grain melting and crushing machine physical method is adopted for pretreating the lignocellulose raw material, so that a cellulose structure wrapped by hemicellulose is opened and a cellulose crystalline structure is simultaneously opened, the method can be used for replacing all acid, alkali and gas explosion treatment methods, the conditions of high temperature and high pressure are not required, no external metal or organic matter such as sulfur is added, the pollution is avoided and the hydrolysis efficiency is high. By adopting the method, no secondary substance inhibiting the growth and the fermentation of yeast, bacteria and anaerobic bacteria is generated, and cellulose, the hemicellulose and lignin are not damaged.

Description

technical field [0001] The invention relates to a method for producing ethanol or acetone butanol by using lignocellulose as raw material. Background technique [0002] At present, lignocellulosic biomass, such as straw, grain, reed, wood and other raw materials are used for renewable energy development. One of the key problems is that cellulose and hemicellulose cannot be quickly degraded or utilized by microorganisms. Sulfase and / or hemicellulase are used for hydrolysis, but the hydrolysis effect is also quite poor. In the past, cellulosic biomass raw materials were pretreated by physical, chemical or a combination of the two methods. In China, corncobs and straws are rich in cellulose and hemicellulose. As a plant species of lignocellulosic biomass, the output of straws can reach 650 million tons, of which the annual output of corncobs can reach 40 million tons. As an important raw material for the conversion of cellulosic biomass. [0003] Previous physical methods of...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C12P7/10C12P7/16C12P7/36C12P19/14C12R1/01C12R1/145C12R1/21C12R1/645
CPCY02E50/16Y02E50/10
Inventor 方诩程少博张杰夏蕊蕊肖林曲音波王明钰
Owner SHANDONG UNIV