Mutant of cellulosic exoglucanase cbh I and viscosity reducer of syrup in corn fuel ethanol fermentation production
A technology of exo-glucanase and cellulose, applied in the directions of fermentation, biofuels, enzymes, etc., can solve the problems of increasing energy consumption of feed drying steam, dark color of DDGS, destruction of nutrients, etc., and achieve excellent enzyme stability and catalytic activity, reducing steam consumption, and improving the effect of primary product yield
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Embodiment 1
[0028] Example 1 Preparation and Properties of Cellulose Exoglucanase CBH I Mutant
[0029] 1. Sequence of the mutant
[0030] The amino acid sequence of Trichoderma reesei cellulose exoglucanase CBH I is shown in SEQ ID NO:1, and the gene cDNA sequence is shown in SEQ ID NO:2.
[0031] After analysis by the molecular simulation software PROPKA software, the tyrosine (Y) at position 68 of the amino acid sequence of Trichoderma reesei cellulosic exoglucanase CBH I was replaced with glycine (G) to obtain mutant Y68G, and the corresponding replacement Codon (substitute GGT for TAC at positions 202-204 in SEQ ID NO:2). For Escherichia coli, the website http: / / www.jcat.de was used for codon optimization, and finally the coding gene of mutant Y68G (SEQ ID NO: 3) was obtained. In addition, the tyrosine (Y) at position 68 of the amino acid sequence of Trichoderma reesei cellulose exoglucanase CBH I was replaced with alanine (A) to obtain mutant Y68A, and the mutation was obtained by...
Embodiment 2
[0044] The preparation of embodiment 2 viscosity reducer
[0045] Viscosity reducers of the following compositions were prepared respectively. The parts in this embodiment are parts by mass. The original cellulosic exoglucanase CBH I in this example, two kinds of mutants Y68G and Y68A, respectively obtain the crude enzyme liquid according to the method in Example 1, then according to Document 1 (Pan Feng et al., Usami Aspergillus Y- 26 The purification and enzymatic properties of cellulase, the method in Nanjing University of Science and Technology, 2001) method to purify each cellulosic exoglucanase and freeze-drying, the specific activity of cellulosic exoglucanase CBH I is 21500U / g, the specific activity of mutant Y68G is 39600U / g, and the specific activity of Y68A is 38400U / g. The information of the remaining enzymes used is shown in Table 2.
[0046] Enzyme information used in the compound viscosity reducer of table 2
[0047] Enzyme name
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Embodiment 3
[0054] Application of embodiment 3 viscosity reducer
[0055] The technological process of corn fuel ethanol fermentation is: corn flour—pulp mixing—adding enzyme preparation and yeast—raw meal fermentation—distillation—dehydration—fuel ethanol. The addition amount of each substance in the fermentation is 2kg of corn flour, 0.1-0.5% of yeast, 20-80U / g corn flour of alpha-amylase, and 100-200U / g corn flour of glucoamylase. Fermentation conditions: material-to-water ratio 1:2-1:5, constant temperature 28-35°C, stirring speed 100-200r / min, fermentation without cooking for 3-6 days. After the fermentation is finished, the fuel ethanol is distilled out, and the distillation waste mash is filtered to obtain a clear liquid. Concentrate the supernatant to a syrup with a concentration (mass percentage of dry matter, the same below) of 29%. Viscosity reduction agent 1 and comparison viscosity reduction agent 1, viscosity reduction agent 4 and comparison viscosity reduction agent 2 in ...
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