Monitoring of Streptomyces peucetius cultivations using FTIR/ATR spectroscopy and quantitative models based on library type data.

Cultivations of Streptomyces peucetius in two types of medium were monitored on-line using a Fourier transform infrared (FTIR) spectrometer combined with an attenuated total reflection probe. The quantitative measurements of the glucose, starch and acetate concentrations were implemented using partial least squares calibration models. These were regressed on spectral and concentration information obtained by adding together single constituent spectra of the main constituents in the medium according to a full factorial design. The accuracy achieved was considered to be satisfactory, with an average root mean square error of prediction of 1.5 g/l for glucose and 0.25 g/l for acetate. The methodology used is considered to be a rapid technique for generation of calibration data, and a step towards the use of library type data for calibration purposes in quantitative FTIR spectroscopy applications in bioprocesses.

On-line measurement of the substrate concentrations in Pichia pastoris fermentations using FT-IR/ATR.

The glycerol and methanol concentrations in Pichia pastoris fermentations were measured on-line using Fourier transform infrared spectroscopy and an attenuated total reflection probe. Partial least squares regression was used to obtain calibration models. The models were regressed on synthetic multi-component spectra and semi-synthetic fermentation broth spectra. These were obtained by spectral addition. The accuracy for the on-line measurement of glycerol, given as standard error of prediction (SEP), was determined to 0.68 g/l, and the SEP of methanol was 0.13 g/l. We show how reliable calibration models are obtained relatively effortlessly by replacing extensive sampling from the reactor with simple mathematical manipulations of the model regression spectra.

Production of recombinant HIV-1 nef protein using different expression host systems: a techno-economical comparison.

Three popular expression host systems Escherichia coli, Pichia pastoris and Drosophila S2 were analyzed techno-economically using HIV-1 Nef protein as the model product. On scale of 100 mg protein, the labor costs corresponded to 52-83% of the manufacturing costs. When analyzing the cost impact of the different phases (strain/cell line construction, bioreactor production, and primary purification), we found that with the microbial host systems the strain construction phase was most significant generating 56% (E. coli) and 72% (P. pastoris) of the manufacturing costs, whereas with the Drosophila S2 system the cell line construction and bioreactor production phases were equally significant (46 and 47% of the total costs, respectively). With different titers and production goal of 100 mg of Nef protein, the costs of P. pastoris and Drosophila S2 systems were about two and four times higher than the respective costs of the E. coli system. When equal titers and bioreactor working volumes (10 L) were assumed for all three systems, the manufacturing costs of the bioreactor production of the P. pastoris and Drosophila S2 systems were about two and 2.5 times higher than the respective costs of the E. coli system.

Production of recombinant HIV-1 Nef (negative factor) protein using Pichia pastoris and a low-temperature fed-batch strategy.

In the present paper we describe the cloning and extracellular expression of the HIV-1 Nef (negative factor) protein utilizing the yeast Pichia pastoris, as well as the successful use of a low-temperature fed-batch strategy for decreasing end-product degradation by proteases. The nef gene in a pPICZalphaA vector was integrated into the genome of three different P. pastoris strains, namely X-33, GS115 and KM71H. On the basis of its efficient growth and production characteristics the wild-type strain (X-33) was found to be the best choice. The decreased end-product degradation at low temperatures was not due to lower amounts of proteases but due to their diminished activity. The yield of biomass from methanol was improved 1.44-fold utilizing the low-temperature strategy compared with the standard fermentation. Purification of histidine-tagged Nef was performed in one step using a Ni(2+)-nitrilotriacetate-Sepharose column. The purified product was characterized by SDS/PAGE, Western blotting, matrix-assisted laser-desorption ionization-time-of-flight MS, reversed-phase HPLC and N-terminal-sequence analysis.