Single step plasmid DNA purification using methacrylate monolith bearing combination of ion-exchange and hydrophobic groups.

Purification of high quantities of human grade plasmid DNA is one of the most intensive production steps. Because of that several methods have been proposed, among them also chromatographic purification using methacrylate monoliths. Recently, a process comprising the combination of hydrophobic interaction (HIC) monolith and ion-exchange monolith was developed. In this work both chemistries were tried to be introduced on a single monolith. Methacrylate monoliths bearing octylamine groups, combination of butyl (C4) grafted methacrylate groups and diethylaminoethyl (DEAE) groups as well as grafted chains bearing both C4 and DEAE groups were prepared. All monoliths were investigated for their ionic and protein capacity and compared to conventional epoxy, C4, and DEAE methacrylate monoliths. Octylamine monolith and monolith bearing combination of C4 grafted methacrylate groups and DEAE groups were found to be the most promising candidates and were further tested for plasmid DNA (pDNA) dynamic binding capacity under ion-exchange (IEX) and HIC binding conditions and ability to separate open circular (OC) from supercoiled (SC) pDNA forms and RNA from pDNA. Since monolith bearing combination of grafted C4 methacrylate groups and DEAE groups was superior in all three tested features, exhibiting pDNA dynamic binding capacity of 4.7 mg/ml under IEX conditions and 2.1mg/ml under HIC conditions, it was used for the development of a single step purification method and tested with pure pDNA as well as with cell lysate. Developed method removed over 99% of RNA, host cell proteins (HCP) and genomic DNA (gDNA) demonstrating capacity to purify around 1.5mg of pDNA/ml of monolith from cell lysate.

Estimation of methacrylate monolith binding capacity from pressure drop data.

Convective chromatographic media comprising of membranes and monoliths represent an important group of chromatographic supports due to their flow-unaffected chromatographic properties and consequently fast separation and purification even of large biological macromolecules. Consisting of a single piece of material, common characterization procedures based on analysis of a small sample assuming to be representative for the entire batch, cannot be applied. Because of that, non-invasive characterization methods are preferred. In this work pressure drop was investigated for an estimation of dynamic binding capacity (DBC) of proteins and plasmid DNA for monoliths with different pore sizes. It was demonstrated that methacrylate monolith surface area is reciprocally proportional to pore diameter and that pressure drop on monolith is reciprocally proportional to square pore size demonstrating that methacrylate monolith microstructure is preserved by changing pore size. Based on these facts mathematical formalism has been derived predicting that DBC is in linear correlation with the square root of pressure drop. This was experimentally confirmed for ion-exchange and hydrophobic interactions for proteins and plasmid DNA. Furthermore, pressure drop was also applied for an estimation of DBC in grafted layers of different thicknesses as estimated from the pressure drop data. It was demonstrated that the capacity is proportional to the estimated grafted layer thickness.

Emulsion templated open porous membranes for protein purification.

Approximately 25 cm×25 cm large sheets of crosslinked highly porous poly(glycidyl methacrylate-co-ethyleneglycol dimethacrylate-co-ethylhexyl methacrylate) membranes with an average thicknesses between 285 and 565 µm were prepared by casting a high internal phase emulsion (HIPE) containing monomers onto glass substrates and subsequent polymerisation. Open cellular porous polyHIPE type membranes were obtained with large pores (cavity) sizes between 3 and 10 µm while interconnecting pores were between 1 and 3 µm. The percentage of ethylhexyl acrylate and ethyleneglycol dimethacrylate influenced the flexibility and morphology of the resulting membranes. Porous membranes were chemically modified with diethylamine to yield functionalised supports for ion exchange chromatography. Cylindrical housings were used for positioning of the membranes and allowing flow of the mobile phase. Pulse experiments were used to study the flow characteristics and a homogeneous flow through the entire area of the membrane was found. Bovine serum albumin was purified by a 8 ml column containing functional membrane in modular shape; dynamic binding capacity was measured to be as high as 45 mg/ml.

Dermatophyte Trichophyton mentagrophytes Produces Cysteine Protease Inhibitor.

The protein inhibitor of cysteine proteases was isolated from an important zoophilic dermatophyte species Trichophyton mentagrophytes (T. mentagrophytes) and partially characterized. The isolation process involved affinity chromatography, followed by ion-exchange chromatography and reverse phase high performance liquid chromatography. The fungal inhibitor appears to exist in a high (24 kDa) and low (12 kDa) molecular mass form. It inhibits proteolytic activity of papain, cathepsins B and L but not of cathepsin H or trypsin. Results of immunoblotting procedures indicate that sera of T. mentagrophytes infected rabbits contain antibodies against higher molecular mass forms of the inhibitor. Since no sequence homology has been found between partial protein sequences of T. mentagrophytes inhibitor and other known cysteine protease inhibitors so far, we can speculate that this inhibitor has some structurally unique characteristics. The T. mentagrophytes inhibitor shares some biochemical similarities (molecular mass, high and low molecular mass forms, inhibitory profiles) with clitocypin from Clitocybe nebularis and macrocypins from Macrolepiota procera.