Method for producing ethanol by carrying out high temperature enzymolysis and fermentation on lignocellulose
A technology of lignocellulose and high-temperature enzymatic hydrolysis, which is applied in the field of ethanol production by high-temperature enzymatic hydrolysis and fermentation of lignocellulose, can solve problems far from reaching the level of industrialization, improve the ability to withstand high temperatures, reduce usage, and reduce feedback inhibitory effect
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Embodiment 1
[0028] The lignocellulosic raw material used in the embodiment of the present invention is dry corn stalk, wherein 38.2wt% of cellulose, 22.1wt% of hemicellulose, 20.2wt% of lignin, and 3.9wt% of ash are pulverized with a pulverizer until the particle size is 1- 5mm. Dilute acid steam explosion was used for pretreatment, the reaction temperature was 190°C, the reaction time was 5min, the solid-liquid ratio was 1:2, and the concentration of dilute sulfuric acid was 2.0wt%. After coming out from the steam explosion device, adjust the pH with NaOH to be 5.0, wherein the dry matter concentration is 32wt%, the cellulose content in the dry matter is 40wt%, and the pretreatment dry matter recovery rate is 96wt%.
[0029] Yeast seed liquid culture medium is 2wt% glucose, 2wt% peptone and 1wt% yeast extract, sterilized at 115°C for 30min for later use. The preparation of yeast seed liquid is divided into 3 stages of cultivation: the first stage uses the inoculation loop to scrape 1-2 ...
Embodiment 2
[0039] The method for producing ethanol by high-temperature enzymatic hydrolysis and fermentation of lignocellulose of the present invention comprises the following contents:
[0040] (1) Combined pretreatment of lignocellulosic raw material corn straw with dilute acid steam explosion to obtain pretreated raw materials;
[0041] (2) Add the pretreated raw materials, cellulase, water and xanthan gum into the enzymolysis tank for pre-enzymolysis, control the dry matter concentration of the enzymolysis system to 15wt%, and control the pre-enzymolysis temperature at 54°C; The residence time of the enzymolysis feed liquid is 8h; the pH of the pre-enzymolysis is 4.5; the addition of xanthan gum is 0.08g / L; The ratio is 5IU / g cellulose;
[0042] (3) After the pre-enzymolysis, the feed liquid is poured into the fermenter, and the temperature-resistant Saccharomyces cerevisiae is added for simultaneous saccharification and fermentation. Synchronous saccharification and fermentation re...
Embodiment 3
[0045] The method for producing ethanol by high-temperature enzymatic hydrolysis and fermentation of lignocellulose of the present invention comprises the following contents:
[0046] (1) Combined pretreatment of lignocellulosic raw material corn straw with dilute acid steam explosion to obtain pretreated raw materials;
[0047] (2) Add pretreated raw materials, cellulase, water and xanthan gum into the enzymolysis tank for preenzymolysis, control the dry matter concentration of the enzymolysis system to 25wt%; control the residence time of the enzymolysis feed solution to 48h The pH of the pre-enzymolysis is 5.5, and the temperature is 62°C; the addition of xanthan gum is 0.24g / L; the addition of the cellulase makes the ratio of the cellulase to the cellulose in the pretreated raw material 25IU / L g cellulose;
[0048] (3) After the pre-enzymolysis, the feed liquid is poured into the fermenter, and the temperature-resistant Saccharomyces cerevisiae is added for simultaneous s...
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