PubMed Health⌕ Search

Biomedical subjects

Anthony Schapman

Publications and source records attributed to Anthony Schapman.

2 recordsLinked to original sources

Expression optimization and purification process development of an engineered soluble recombinant mouse linker of activation of T cells using surface enhanced laser desorption/ionization-mass spectrometry.

Protein purification development is the bottleneck of recombinant protein production therefore there is a need to shorten process development and monitoring. Surface enhanced laser desorption/ionization-mass spectrometry (SELDI-MS) was evaluated to optimize the expression and to develop the purification of a recombinant mouse protein: a transmembrane adaptor involved in T cell receptor signaling named "linker for activation of T cells" (LAT). The protein was expressed as a soluble form (S-LAT) in three strains of Escherichia coli: BL21 (DE3), Rosetta (DE3), and BL21 (DE3) pLys S. The expression of S-LAT was monitored on immobilized metal affinity chromatography (IMAC) ProteinChip arrays. The highest level of expression was found in Rosetta (DE3) with a C-terminal construct after induction at 37 degrees C. The purification scheme was elucidated using SELDI-MS: S-LAT was efficiently captured on an IMAC ProteinChip array saturated with nickel ions (Ni(2+)) and then fractionated on a Q ProteinChip array. These conditions were directly transferred to IMAC-Ni(2+) HyperCel and Q Ceramic HyperD F chromatography sorbents. After these two purification steps, S-LAT was estimated to be more than 80% pure, confirming a very good match between array and sorbent. Finally, a peptide mapping was performed on a hydrophobic array after in gel trypsin digest, verifying that the purified protein was the mouse LAT. This is the first report of a protocol for the production and purification of S-LAT. The selection of the best expression and purification strategy along with the identification were enabled in 5 days with less than 5 mL of soluble fraction of crude culture samples.

Adaptor Proteins, Signal Transducing↗

Endostatin capture from Pichia pastoris culture in a fluidized bed. From on-chip process optimization to application.

One of the characteristics of the methylothrophic yeast Pichia pastoris is its ability to grow to a very high cell density. Biomass concentrations of 300-400 g wet mass/l are common. It is therefore obvious that the recovery processes of extracellular proteins from this microorganism should take into account the effect of high biomass content. Separation by filtration and/or centrifugation is possible but these steps are cumbersome and can affect the protein recovery. The use of fluidized beds is attractive proteins capture option since it eliminates the biomass while capturing the desired protein. Zirconia-based resins possess unique properties which make them appropriate for processing high biomass concentrations in an expanded bed mode. The beads are particularly heavy (density is 3.2 g/ml) and small (75 microm) and therefore can accommodate high fluidization velocity and high mass transport. Specific operating conditions for effective capture of expressed protein have to be determined. This determination is generally time consuming and requires relatively large amount of feedstock for the lab trials. To avoid multiple chromatographic trials in columns, optimal conditions of adsorption and elution were determined by ProteinChip technology coupled with mass spectrometry. This technology involves flat chip surfaces functionalized as chromatographic beads where it is possible to adsorb and desorb proteins. Four different functional groups (strong anion-exchange, weak cation-exchange, hydrophobic and metal chelate) were tested and the retained proteins were analyzed directly by mass spectrometry. The weak cation-exchange group was chosen for further work. The Zirconia-based weak cation-exchange sorbent (CM HyperZ) was evaluated for binding capacity in a packed column and then for capturing endostatin from crude feed stock. Based on the previously determined conditions; 45 l of culture containing approximately 15 kg of biomass (wet mass) and 3 g endostatin were applied on an expanded bed at a flow-rate of 535 cm/h, yielding 80% of the endostatin and removing approximately 80% of foreign proteins.

Cation Exchange Resins↗