For the expression of IgG1, genes encoding VH and VL were amplified from the phage clones, cloned into a mammalian expression vector, and transfected into HEK293F cells. Then, IgG1 was purified by Protein A affinity chromatography as described previously [68 (link)]. Then the eluate containing IgG1 was subjected to gel filtration chromatography. A total of 4 mg of IgG1 was injected at a flow rate of 1 mL/min and purified by gel filtration using a XK16/100 column packed with Superdex 200 pg at pH 7.4 (ÄKTA pure, GE Healthcare). The chromatogram was recorded at a UV absorbance of 280 nm. The fractions containing IgG1 were pooled by collection criteria and concentrated.
Hek293f cell
HEK293F cells are an established human embryonic kidney cell line commonly used for recombinant protein production and viral vector manufacturing. These cells are adherent and can be adapted to grow in suspension culture. HEK293F cells provide a well-characterized system for research and development purposes.
Lab products found in correlation
231 protocols using hek293f cell
Production and Purification of IgG1 Antibodies
For the expression of IgG1, genes encoding VH and VL were amplified from the phage clones, cloned into a mammalian expression vector, and transfected into HEK293F cells. Then, IgG1 was purified by Protein A affinity chromatography as described previously [68 (link)]. Then the eluate containing IgG1 was subjected to gel filtration chromatography. A total of 4 mg of IgG1 was injected at a flow rate of 1 mL/min and purified by gel filtration using a XK16/100 column packed with Superdex 200 pg at pH 7.4 (ÄKTA pure, GE Healthcare). The chromatogram was recorded at a UV absorbance of 280 nm. The fractions containing IgG1 were pooled by collection criteria and concentrated.
Rhesus Macaque Antibody Production
Recombinant Protein Production and Antibody Purification
Monoclonal Antibody Production Protocol
Recombinant Anti-TSH Antibody Production
Purification of Recombinant Trimeric HA
Purification of Mouse and Chimeric Antibodies
Recombinant Fab and PD-1 Protein Expression
Plasmid pMax‐PD‐1 was transiently transfected into HEK293F cells (Thermo Fisher) for protein expression. The supernatant was collected, and the PD‐1 was purified by protein A, followed by treatment with TEV Protease to remove the Fc tag. Then, the Fc‐removed PD‐1 was further purified with Superdex 200 (GE Healthcare) in a buffer containing 20 m
Transient Expression of A2M Variants
Example 9
A2M variants were expressed in HEK293F cells (Gibco) by transient transfection of each construct in suspension cells. Cells were grown to a density of 550,000 cells/mL in a Erlenmeyer cell culture flask containing 20 mL of FreeStyle F17 medium (Invitrogen) containing 1× GlutaMax (Gibco) on a rotator at a speed of 125 rpm inside a 37° C. incubator containing an 8% CO2/air mixture. Cells were transfected by mixing 20 μg of plasmid DNA of each construct (wild-type or variant) in a 1:2 (w/v) ratio with TransIT Pro plus 10 μL TransIT Boost (Mirus) 15 minutes before addition to media. Cells were maintained in the same conditions for three days after transfection before the media containing secreted recombinant protein was removed for protein purification (
Transient Transfection of A2M Variants in HEK293F Cells
Example 9
A2M variants were expressed in HEK293F cells (Gibco) by transient transfection of each construct in suspension cells. Cells were grown to a density of 550,000 cells/mL in a Erlenmeyer cell culture flask containing 20 mL of FreeStyle F17 medium (Invitrogen) containing 1× GlutaMax (Gibco) on a rotator at a speed of 125 rpm inside a 37° C. incubator containing an 8% CO2/air mixture. Cells were transfected by mixing 20 μg of plasmid DNA of each construct (wild-type or variant) in a 1:2 (w/v) ratio with TransIT Pro plus 10 μL TransIT Boost (Mirus) 15 minutes before addition to media. Cells were maintained in the same conditions for three days after transfection before the media containing secreted recombinant protein was removed for protein purification (
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