Thermodynamic modelling of supercritical water gasification: investigating the effect of biomass composition to aid in the selection of appropriate feedstock material.

A process model developed in Aspen Plus®, was used for the thermodynamic modelling of supercritical water gasification (SCWG) using a wide variety of biomass materials as feedstock. The influence of the composition of the biomass material (in terms of carbon, hydrogen and oxygen content) on various performance indicators (such as gas yields, cold gas efficiency, calorific value of product gas and heat of reaction), were determined at various temperatures (600, 700 and 800°C) and biomass feed concentrations (5, 15 and 25wt.%). Generalised contour plots, based on the biomass composition, were developed for these performance indicators to provide the thermodynamic limits at various operating conditions. These plots can aid in the selection or screening of potential biomass materials and appropriate operating conditions for SCWG prior to conducting experimental work.

Amino acid supplementation, controlled oxygen limitation and sequential double induction improves heterologous xylanase production by Pichia stipitis.

Heterologous endo-beta-1,4-xylanase was produced by Pichia stipitis under control of the hypoxia-inducible PsADH2-promoter in a high-cell-density culture. After promoter induction by a shift to oxygen limitation, different aeration rates (oxygen transfer rates) were applied while maintaining oxygen-limitation. Initially, enzyme production was higher in oxygen-limited cultures with high rates of oxygen transfer, although the maximum xylanase activity was not significantly influenced. Amino acid supplementation increased the production of the heterologous endo-beta-1,4-xylanase significantly in highly aerated oxygen-limited cultures, until glucose was depleted. A slight second induction of the promoter was observed in all cultures after the glucose had been consumed. The second induction was most obvious in amino acid-supplemented cultures with higher oxygen transfer rates during oxygen limitation. When such oxygen-limited cultures were shifted back to fully aerobic conditions, a significant re-induction of heterologous endo-beta-1,4-xylanase production was observed. Re-induction was accompanied by ethanol consumption. A similar protein production pattern was observed when cultures were first grown on ethanol as sole carbon source and subsequently glucose and oxygen limitation were applied. Thus, we present the first expression system in yeast with a sequential double-inducible promoter.

Amino acid supplementation improves heterologous protein production by Saccharomyces cerevisiae in defined medium.

Supplementation of a chemically defined medium with amino acids or succinate to improve heterologous xylanase production by a prototrophic Saccharomyces cerevisiae transformant was investigated. The corresponding xylanase production during growth on ethanol in batch culture and in glucose-limited chemostat culture were quantified, as the native ADH2 promoter regulating xylanase expression was derepressed under these conditions. The addition of a balanced mixture of the preferred amino acids, Ala, Arg, Asn, Glu, Gln and Gly, improved both biomass and xylanase production, whereas several other individual amino acids inhibited biomass and/or xylanase production. Heterologous protein production by the recombinant yeast was also improved by supplementing the medium with succinate. The production of heterologous xylanase during growth on ethanol or glucose could thus be improved by supplementing metabolic precursors in the carbon- or nitrogen-metabolism.

Comparison of three expression systems for heterologous xylanase production by S. cerevisiae in defined medium.

The influence of the auxotrophic deficiencies of the host strain and expression vector selection on the production of a heterologous protein was investigated. Heterologous xylanase production by two prototrophic S. cerevisiae transformants, containing either a plasmid-based, YEp-type expression system or an integrative, YIp-type expression system, were compared with production by an auxotrophic transformant, containing an identical YEp-type expression system, in batch and continuous cultivation, using a chemically defined medium. Heterologous xylanase production by the auxotrophic strains in defined medium was critically dependent on the availability of amino acids, as extracellular xylanase production increased dramatically when amino acids were over-consumed from the medium to the point of saturating the cell. Saturation with amino acids, indicated by an increased leakage of amino acids from the cell, was thus a prerequisite for high level of heterologous protein production by the auxotrophic strain. Maximal xylanase production levels by the auxotrophic strain corresponded to the levels obtained with a similar prototrophic strain during cultivation in defined medium without amino acids. Superfluous auxotrophic markers thus had a strong deleterious effect on heterologous protein production by recombinant yeasts, and the use of such strains should be limited to initial exploratory investigations. The increased copy number and foreign gene dosage of the YEp-based expression vector, stabilized by the ura3 fur1 autoselection system, significantly improved production levels of heterologous xylanase, compared to the YIp system, which is based on a single integration into the yeast genome. No evidence was found of the possible saturation of the host secretory capacity by multicopy overexpression. Stable production of heterologous xylanase at high levels by the prototrophic YEp-based recombinant strain, compared to the YIp system, was demonstrated.