A novel alkaline oxidation pretreatment for spruce, birch and sugar cane bagasse.

Alkaline oxidation pretreatment was developed for spruce, birch and sugar cane bagasse. The reaction was carried out in alkaline water solution under 10 bar oxygen pressure and at mild reaction temperature of 120-140°C. Most of the lignin was solubilised by the alkaline oxidation pretreatment and an easily hydrolysable carbohydrate fraction was obtained. After 72 h hydrolysis with a 10 FPU/g enzyme dosage, glucose yields of 80%, 91%, and 97%, for spruce, birch and bagasse, respectively, were achieved. The enzyme dosage could be decreased to 4 FPU/g without a major effect in terms of the hydrolysis performance. Compared to steam explosion alkaline oxidation was found to be significantly better in the conditions tested, especially for the pretreatment of spruce. In hydrolysis and fermentation at 12% d.m. consistency an ethanol yield of 80% could be obtained with both bagasse and spruce in 1-3 days.

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.

Production of xylitol from D-xylose by recombinant Lactococcus lactis.

The D-xylose reductase from Pichia stipitis CBS 5773 and the xylose transporter from Lactobacillus brevis ATCC 8287 were expressed in active form in Lactococcus lactis NZ9800. Xylitol production was investigated using non-growing recombinant cells in high cell-density under microaerobic conditions in the presence of xylose and glucose. Besides xylose, the recombinant strain with xylose reductase activity reduced l-arabinose and D-ribose in significant extent to the corresponding pentitols. The ratio of xylitol produced per glucose consumed was almost 10-fold higher under glucose limitation than the ratio in the presence of excess initial glucose. The co-expression of the xylose transporter with the xylose reductase did not increase the efficiency of xylitol production appreciably when compared to the strain in which only the xylose reductase gene was expressed. A fed-batch experiment with high initial xylose concentration (160 gl(-1)) under glucose limitation was carried out using the strain co-expressing xylose reductase and xylose transporter genes. The xylitol yield from xylose was 1.0 mol mol(-1) and the ratio of xylitol produced per glucose consumed was 2.5 mol mol(-1). The volumetric productivity was 2.72 gl(-1)h(-1) at 20 h. Of the xylose initially present, 34% was consumed. Analysis of the fermentation metabolites revealed a shift from homolactic to mixed acid fermentation at early stages of the experiment.

Improved mannitol production by a random mutant of Leuconostoc pseudomesenteroides.

A mutant of Leuconostoc pseudomesenteroides ATCC12291 that was unable to grow on fructose was constructed by chemical mutagenesis. The fructose uptake of this mutant, designated as BPT143, was unaltered and allowed fructose still to be converted into mannitol when glucose was present in the growth medium. The mutant grew and consumed fructose faster than the parent strain when grown in a medium containing both glucose and fructose. The specific activity of fructokinase, the enzyme involved in phosphorylation of fructose to fructose-6-phosphate, was decreased to about 10% of that of the parent strain, and resulted in a reduced leakage of fructose into the phosphoketolase (PK) pathway. The yield of mannitol from fructose was improved from 74 to 86 mol%. The increased fructose consumption rate and higher mannitol yield of the mutant also resulted in improvement of volumetric mannitol productivity. In addition, isolation and characterization of the wild type L. pseudomesenteroides fructokinase gene (fruK) was performed. DNA sequence analysis of the fruK gene region of BPT143 revealed only one silent mutation which does not explain the highly reduced fructokinase activity of the mutant. The genetic characterization of fruK was completed by analyzing the expression, size and 5' end of fruK transcripts. Expression data with BPT143, revealing absence of fruK transcripts, was in accordance with the reduced fructokinase activity of the mutant.

Xylanase production by Trichoderma reesei Rut C-30 grown on L-arabinose-rich plant hydrolysates.

The suitability of L-arabinose-rich plant hydrolysates as carbon sources and inducers of xylanase production in Trichoderma reesei Rut C-30 was tested. Significantly higher xylanase activities were obtained in cultures on oat husk and sugar beet pulp hydrolysates than on lactose. In batch culture with oat husk hydrolysate and lactose, the xylanase activity was about 9 times higher ( approximately 510 IU/ml) than in lactose ( approximately 60 IU/ml). Even higher xylanase activity ( approximately 630 IU/ml) was obtained when the batch cultivations were done on sugar beet pulp hydrolysate and lactose. In a fed-batch culture using oat husk hydrolysate-lactose the xylanase activity was as high as 1350 IU/ml in 4 days. The cellulase production clearly decreased when T. reesei was cultured on both hydrolysates compared to the cultivation on lactose. Moreover, the relative amounts of the xylanases I-III were similar regardless the used carbon source.

Metabolic engineering of Lactobacillus fermentum for production of mannitol and pure L-lactic acid or pyruvate.

For production of mannitol in combination with pure L-lactic acid or pyruvate, the D- and L-lactate dehydrogenase genes (ldhD and ldhL) of a mannitol-producing Lactobacillus fermentum strain were cloned and stepwise inactivated. For inactivation of both ldh genes by a gene replacement technique, deletion constructs removing a 0.4-kb fragment from the promoter and the 5' end region of the ldh genes were used. The first inactivation mutant, designated L. fermentum GRL1030, carried the deletion in ldhD (DeltaldhD). A double mutant, DeltaldhD-DeltaldhL, was constructed by the inactivation of the ldhL gene of strain GRL1030, resulting in strain L. fermentum GRL1032. The correctness of the both mutants was confirmed at the DNA level by polymerase chain reaction, as shown by the absence of ldh transcripts by northern blotting and as a lack of the corresponding enzyme activity. In bioreactor cultivations, the single mutant GRL1030 produced mannitol and L-lactic acid as expected. Mannitol and lactic acid yields and productivities were practically unaffected by deletion of the ldhD gene. The double mutant GRL1032 produced mannitol and pyruvate as expected. However, although the yield of mannitol from fructose remained high, its volumetric productivity was reduced. The double mutation negatively affected the glucose consumption rate, resulting in reduced cellular growth. In addition to pyruvate, the double mutant produced 2,3-butanediol. More surprisingly, some lactic acid was still produced.

High-level production of D-mannitol with membrane cell-recycle bioreactor.

Ten heterofermentative lactic acid bacteria were compared in their ability to produce D-mannitol from D-fructose in a resting state. The best strain, Leuconostoc mesenteroides ATCC-9135, was examined in high cell density membrane cell-recycle cultures. High volumetric mannitol productivity (26.2 g l(-1) h(-1)) and mannitol yield (97 mol%) were achieved. Using the same initial biomass, a stable high-level production of mannitol was maintained for 14 successive bioconversion batches. Applying response surface methodology, the temperature and pH were studied with respect to specific mannitol productivity and yield. Moreover, increasing the initial fructose concentration from 100 to 120 and 140 g l(-1) resulted in decreased productivities due to both substrate and end-product inhibition of the key enzyme, mannitol dehydrogenase (MDH). Nitrogen gas flushing of the bioconversion media was unnecessary, since it did not change the essential process parameters.