1,2-diarachidoyl-sn-glycero-3-phosphocholine (DAPC) (>99%) and used without further purification unless otherwise stated. Expression vectors of pFL-B62cl were from GeneCopoeia Inc. (USA). Escherichia coli SHuffle T7 Express Competent cells were purchased from New England BioLabs (Beijing, China). IPTG (isopropyl β-D-1-thiogalactopyranoside) and Ampicillin were from Sangon Biotech, Shanghai Co., Ltd. (Shanghai, China). All other reagents were of analytical grade.
Isopropyl β d 1 thiogalactopyranoside (iptg)
IPTG (Isopropyl β-D-1-thiogalactopyranoside) is a synthetic chemical compound commonly used in molecular biology and genetic engineering. It serves as an inducer, activating the expression of genes that are under the control of the lac operon. IPTG mimics the natural inducer, allolactose, and binds to the lac repressor, causing it to dissociate from the operator region of the lac operon, thereby allowing transcription of the downstream genes.
Lab products found in correlation
68 protocols using isopropyl β d 1 thiogalactopyranoside (iptg)
Phospholipid Synthesis and Purification
1,2-diarachidoyl-sn-glycero-3-phosphocholine (DAPC) (>99%) and used without further purification unless otherwise stated. Expression vectors of pFL-B62cl were from GeneCopoeia Inc. (USA). Escherichia coli SHuffle T7 Express Competent cells were purchased from New England BioLabs (Beijing, China). IPTG (isopropyl β-D-1-thiogalactopyranoside) and Ampicillin were from Sangon Biotech, Shanghai Co., Ltd. (Shanghai, China). All other reagents were of analytical grade.
Nicotine Synthesis and Plasmid Construction
Cloning and Purification of ORF41 Phage Protein
Recombinant Protein Expression and Purification
Recombinant NoV P Protein Expression
Synthesis of Aromatic Compounds
Nicotine Biosynthesis Pathway Characterization
Preculture and Aerobic Cultivation of C. glutamicum
For aerobic growth, cells were washed twice with CGXIIB medium and used to inoculate 50 ml of CGXIIA medium with 20 g L−1 of xylose or glucose to an initial OD600 = 0.8, and cultured in 500 mL shake flasks at 30 °C and 220 rpm on a rotary shaker.
A two-stage process was performed for succinate production. When the cultures reached an OD600 of 20, the cells were harvested by centrifugation (5 000×g, 4 °C, 10 min), washed with CGXIIB medium. An appropriate amount of washed cells was suspended in 25 mL CGXIIB medium with the indicated sugars and 200 mM sodium bicarbonate, and the cell suspension was cultured in 50 mL serum bottles at 30 °C and 220 rpm on a rotary shaker. To prevent acidification, 30 g L−1 of magnesium carbonate hydroxide (4MgCO3·Mg(OH)2·5H2O) was added as a buffering agent. For induction, isopropyl β-
Bacterial Cultivation and Antibiotic Use
Recombinant Protein Expression and Antioxidant Assays
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