A method for enzymatically preparing 4-hydroxyphenylacetaldehyde
A technology of hydroxybenzene and acetaldehyde, which is applied in the field of enzymatic production of 4-hydroxyphenylacetaldehyde, can solve problems such as difficult scale-up production, difficult large-scale production, severe reaction conditions, etc., and achieve high reaction yield, low production cost, specific effect
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Embodiment 1
[0026] Embodiment 1: construction of engineering bacteria
[0027] According to the Escherichia coli K12 tynA gene sequence (SEQ ID No.1), the upstream primer F-tynA containing the BamH I restriction site was designed: 5'-AAGGATCCATGGGAAGCCCCCTCTCTGTATTC-3', and the downstream primer R- containing the EcoR I restriction site tynA: 5'-AACTCGAGTCACTTATCTTTCTTCAGCGCC-3'. The genomic DNA of Escherichia coli K12 was extracted by the bacterial genomic DNA extraction kit, and the genomic DNA was used as a template for PCR amplification. The PCR reaction system included 10×ExTaq buffer (Mg 2+ Plus) 5 μL, dNTPs mixture 4.0 μL, TaKaRa ExTaq 0.5 μL, template 1.0 μL, upstream and downstream primers 1.0 μL each, with dd H 2 O to make up to 50 μL. The PCR reaction parameters were: 94°C for 30s, 60°C for 30s, 72°C for 1min, and after 30 cycles, 72°C for 10min. PCR amplified products were detected with 1% agarose gel, and the target DNA fragment was purified with AxyPrep DNA Gel Recovery K...
Embodiment 2
[0028] Example 2 Production of primary amine oxidase by fermentation of recombinant bacteria and enzymatic conversion of tyramine to produce 4-hydroxyphenylacetaldehyde
[0029] (1) Insert the constructed genetically engineered bacteria into LB slant medium and cultivate at 37°C for 16h;
[0030] (2) Connect 1 ring of slant strains to LB liquid seed medium, shake and culture at 37°C and 200r / min for 6h;
[0031] (3) 3.0L medium is loaded into the 5L fermenter, the seed liquid is inserted into the fermentation medium with 8% seed quantity, the initial speed is 200r / min, the initial ventilation flow rate is 1.5L / min, and the speed is adjusted as the cell concentration increases In order to maintain the dissolved oxygen value above 20% with the ventilation flow rate, adjust the pH value at 7.0 with 25% ammonia water, culture at 37°C for 6 hours and cool down to 30°C for expression. During the fermentation process, 500g / L glycerol solution was added to maintain the glucose concen...
Embodiment 3
[0034] Example 3 Production of primary amine oxidase by fermentation of recombinant bacteria and enzymatic conversion of tyramine to produce 4-hydroxyphenylacetaldehyde
[0035] (1) Insert the genetically engineered bacteria constructed in Example 1 into LB slant medium and cultivate at 37° C. for 15 hours;
[0036] (2) Connect 1 ring of slant strains to LB liquid seed medium, shake and culture at 37°C and 200r / min for 8h;
[0037] (3) 3.0L medium is loaded into the 5L fermenter, the seed solution is inserted into the fermentation medium with a volume ratio of 7%, the initial rotation speed is 200r / min, and the initial ventilation flow rate is 1.5L / min. Adjust the rotation speed and ventilation flow to maintain the dissolved oxygen value above 20% air saturation, adjust the pH value to be stable at 7.0 with 25% ammonia water in mass to volume ratio, incubate at 37°C for 7 hours and cool down to 28°C for expression. Add 500g / L glycerol solution to maintain glycerol concentrati...
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