Engineering Pichia pastoris for improved NADH regeneration: A novel chassis strain for whole-cell catalysis

  1. Martina Geier1,
  2. Christoph Brandner1,
  3. Gernot A. Strohmeier1,2,
  4. Mélanie Hall3,
  5. Franz S. Hartner4,5 and
  6. Anton Glieder5

1Austrian Centre of Industrial Biotechnology (ACIB GmbH), Petersgasse 14, Graz, 8010, Austria
2Institute of Organic Chemistry, Graz University of Technology, Stremayrgasse 9, Graz, 8010, Austria
3Department of Chemistry, University of Graz, Heinrichstrasse 28, Graz, 8010, Austria

4Sandoz GmbH, Biochemiestrasse 10, 6250, Kundl, Austria
5Institute of Molecular Biotechnology, Graz University of Technology, Petersgasse 14, Graz, 8010, Austria

  1. Corresponding author email

This article is part of the Thematic Series "Sustainable catalysis".

Guest Editor: N. Turner
Beilstein J. Org. Chem. 2015, 11, 1741–1748. doi:10.3762/bjoc.11.190
Received 03 Jun 2015, Accepted 26 Aug 2015, Published 25 Sep 2015

Abstract

Many synthetically useful reactions are catalyzed by cofactor-dependent enzymes. As cofactors represent a major cost factor, methods for efficient cofactor regeneration are required especially for large-scale synthetic applications. In order to generate a novel and efficient host chassis for bioreductions, we engineered the methanol utilization pathway of Pichia pastoris for improved NADH regeneration. By deleting the genes coding for dihydroxyacetone synthase isoform 1 and 2 (DAS1 and DAS2), NADH regeneration via methanol oxidation (dissimilation) was increased significantly. The resulting Δdas1 Δdas2 strain performed better in butanediol dehydrogenase (BDH1) based whole-cell conversions. While the BDH1 catalyzed acetoin reduction stopped after 2 h reaching ~50% substrate conversion when performed in the wild type strain, full conversion after 6 h was obtained by employing the knock-out strain. These results suggest that the P. pastoris Δdas1 Δdas2 strain is capable of supplying the actual biocatalyst with the cofactor over a longer reaction period without the over-expression of an additional cofactor regeneration system. Thus, focusing the intrinsic carbon flux of this methylotrophic yeast on methanol oxidation to CO2 represents an efficient and easy-to-use strategy for NADH-dependent whole-cell conversions. At the same time methanol serves as co-solvent, inductor for catalyst and cofactor regeneration pathway expression and source of energy.

Keywords: bioreduction; cofactor regeneration; dihydroxyacetone synthase; methanol utilization pathway; whole-cell biotransformation

Introduction

Bioreductions represent a sustainable strategy to obtain enantiopure molecules which serve as chiral building blocks for fine chemicals and drugs [1,2]. Such reactions are catalyzed by oxidoreductases, which mainly depend on nicotinamide cofactors as electron donors and acceptors. As these cofactors are required in stoichiometric amounts to drive the reaction to completion and the simple addition of these compounds is not acceptable from an economical point of view, efficient in situ regeneration of the consumed cofactor is required. During the recent years, a broad range of cofactor regeneration systems based on enzymatic, chemical, photochemical or electrochemical processes have been developed [3].

In living (growing) cells, NAD(P)H can be recycled via the cellular metabolism of a co-substrate such as glucose. Alternatively, cofactor regeneration enzymes such as D-glucose-6-phosphate dehydrogenase, formaldehyde dehydrogenase and formate reductase can be co-expressed ensuring cofactor supply also in non-growing, resting cells. In addition to the cofactor supply, the application of whole cells circumvents time-consuming enzyme isolation and purification steps and improves enzyme stabilities during a process [4]. Nowadays, efforts are made to further increase the cofactor availability within cells and to allow the use of alternative and cheaper co-substrates by strain engineering [1,5-7].

Here, we present a novel, engineered platform strain for the use in whole-cell bioreductions and NADH-dependent biosynthetic pathways based on the methylotrophic yeast Pichia pastoris (Komagataella phaffi). P. pastoris is well known as an excellent host for recombinant protein production [8,9]. More recently it also attracted attention as a suitable whole-cell catalyst [10-15]. The target of the presented engineering approach is the methanol utilization (MUT) pathway, which is schematically depicted in Figure 1. This pathway enables methylotrophic yeasts to use methanol as sole carbon source [16]. In the initial step, methanol is oxidized by alcohol oxidase (AOX) to formaldehyde, which is further metabolized either in the assimilatory or in the dissimilatory pathway. In the latter one, formaldehyde spontaneously reacts with glutathione to S-hydroxymethylglutathione which is oxidized in a first step by the glutathione- and NAD+-dependent enzyme formaldehyde dehydrogenase (FLD) to S-formylglutathione. S-Formylglutathione hydrolase (FGH) then hydrolyses this compound to formate and glutathione. In a second NAD+-dependent step, formate is oxidized to CO2 by formate dehydrogenase (FDH). Thus, 2 equivalents of the cofactor NADH are generated via the dissimilatory pathway and full oxidation of the single carbon molecule methanol. Alternatively, in a simplified model formaldehyde is condensed with D-xylulose-5-phosphate and subsequently converted into dihydroxyacetone and D-glyceraldehyde-3-phosphate by dihydroxyacetone synthase (DAS), thereby contributing to biomass production on methanol.

[1860-5397-11-190-1]

Figure 1: Simplified schematic representation of the methanol utilization pathway in Pichia pastoris. The main pathways and the respective enzymes are shown. AOX: alcohol oxidase; FLD: glutathione-dependent formaldehyde dehydrogenase; FGH: S-formylglutathione hydrolase; FDH: formate dehydrogenase; CAT: catalase; DAS: dihydroxyacetone synthase; DAK: dihydroxyacetone kinase; DHA: dihydroxyacetone; GAP: D-glyceraldehyde-3-phosphate; DHAP: dihydroxyacetone phosphate; FBP: D-fructose 1,6-bisphosphate; F6P: D-fructose 6-phosphate; Xu5P: D-xylulose 5-phosphate. By deleting dihydroxyacetone synthase the dissimilatory pathway leading to the formation of NADH is strengthened.

Modifying the dissimilatory part of the MUT pathway has already been shown to improve the substrate conversion by NADH-dependent enzymes in P. pastoris [7]. Over-expression of the formaldehyde dehydrogenase, which was identified as the main bottleneck for an efficient cofactor recycling via the dissimilatory pathway, significantly improved the production rates of NADH-dependent whole-cell biotransformations. In contrast, the present study focuses on redirecting the flux in the MUT pathway by disrupting the assimilation pathway. Thus, the co-substrate methanol should be exclusively redirected to cofactor regeneration in theory, increasing the available NADH concentration in whole-cell biotransformations, while cells should not be able to grow any more if methanol is the sole carbon source.

Results and Discussion

Construction of knock-out strains

The assimilatory pathway was disrupted by the knock-out of dihydroxyacetone synthase. In contrast to other methylotrophic yeasts, P. pastoris has two genes encoding two isoforms of this enzyme (DAS1 and DAS2) [17,18]. Therefore, three knock-out strains were generated to investigate their impact on cofactor regeneration: the single knock-outs Δdas1 and Δdas2 as well as the double knock-out Δdas1 Δdas2.

The targeted gene disruption was accomplished with knock-out cassettes as described earlier [19,20]. The cassettes were harboring a ZeocinTM resistance marker for the selection of integrative transformants and the FLP recombinase system [21] to enable marker recycling. Thereby, marker-free knock-out strains were obtained which only have one 34 bp FLP recombination target sequence (FRT) left in the targeted locus. The cassettes were designed such that the complete coding sequence including the start and stop codons of the corresponding DAS gene was deleted as schematically depicted in Figure 2. In the case of Δdas1 Δdas2, the coding sequences of both genes were deleted in one step, thereby also removing HOB3, coding for a hypothetical guanosine nucleotide exchange factor.

[1860-5397-11-190-2]

Figure 2: Representation of the genomic region coding for dihydroxyacetone synthases. The DAS1 and DAS2 coding sequences are located in close proximity on chromosome 3 in opposite direction. The two genes are separated by a short sequence encoding a hypothetical guanosine nucleotide exchange factor (HOB3). The target sites for the respective das knock-out cassettes are indicated schematically.

Characterization of knock-out strains

In a first step, the generated das knock-out strains were characterized by determining their specific growth rate on different carbon sources. As expected, the growth of the single and double knock-out strains on D-glucose and glycerol was not significantly impaired, showing growth rates in the same order of magnitude as the wild type strain (Table 1). A distinct phenotype was observed when methanol was used as the sole carbon source for growth. A slight, but residual growth was observed for the double knock-out strain, although both dihydroxyacetone synthase genes, that are linking methanol to biomass production, were deleted. In the course of 38 h, the optical density of the P. pastoris Δdas1 Δdas2 cultures on methanol doubled. This remaining carbon flux into cellular metabolism might also enable the continuation of protein expression and thus biocatalyst production, while still maintaining a strong methanol flux towards oxidation to CO2 and NADH regeneration.

Table 1: Specific growth rates of P. pastoris CBS7435 and generated das knock-out strains on different carbon sources. Values represent mean values ± standard deviations of the growth rate during the exponential growth phase determined in biological triplicates.

Strain Growth rate [h−1]
  D-Glucose Glycerol Methanol
P. pastoris CBS7435 0.25 ± 0.03 0.19 ± 0.05 0.15 ± 0.03
P. pastoris CBS7435 Δdas1 0.23 ± 0.06 0.21 ± 0.04 0.12 ± 0.03
P. pastoris CBS7435 Δdas2 0.23 ± 0.03 0.20 ± 0.02 0.09 ± 0.01
P. pastoris CBS7435 Δdas1 Δdas2 0.26 ± 0.03 0.20 ± 0.04 0.01 ± 4 × 10−3

Deleting only one isoform of the dihydroxyacetone synthase did not have such a severe impact on the methanol depending growth of P. pastoris. The growth rates were reduced by ~20% and by ~40% for the Δdas1 and Δdas2 single knock-out strains, respectively.

The behavior of the das knock-out strains in heterologous protein production was tested by expressing green fluorescent protein (GFP) under the control of the AOX1 promoter (PAOX1), which is the most prominent, methanol inducible promoter for P. pastoris.

A possible negative effect on PAOX1 driven protein expression might arise from changes in the energy metabolism due to the interrupted input into the pentose phosphate cycle. In addition, a possible accumulation of methanol oxidation products due to the lack of the two key metabolizing enzymes might be unfavorable for recombinant protein production. However, as shown in Figure 3, the PAOX1 driven expression of GFP was not negatively affected by deleting the DAS gene(s). In fact, the obtained expression levels in the generated single knock-out strains were increased up to ~30% in comparison to the wild type P. pastoris strain. These findings are of importance for the use of the knock-out strains in whole-cell processes, as impairments in recombinant protein production, i.e., the production of the actual biocatalyst, would reduce its applicability.

[1860-5397-11-190-3]

Figure 3: Relative expression levels of the green fluorescent protein (GFP) in the das knock-out strains. GFP expression obtained in the wild type P. pastoris strain indicated as relative fluorescence units per OD600 unit was set as 100%. GFP fluorescence was measured after 70 h of methanol induction. The shown values represent mean values ± standard deviations of 40 individual transformants.

NADH-dependent biotransformations performed in knock-out strains

To evaluate the NADH regeneration potential of the generated knock-out strains, they were employed as hosts in whole-cell bioreductions based on the 2,3-butanediol dehydrogenase from S. cerevisiae YAL060W (BDH1). This enzyme was shown to specifically use NADH as cofactor, displaying high turnover numbers in the reduction of racemic acetoin (kcat = 98,000 min−1) [22].

In an initial screening step, BDH1 transformants in the respective wild type and knock-out backgrounds were evaluated by performing acetoin conversions in the 96 well deep-well format. After biomass production on a D-glucose containing medium, methanol was fed as the sole carbon source to induce the production of the BDH1 enzyme and to induce the dissimilatory pathway. After 12 hours of induction acetoin was added to the growing cells as substrate in addition to the co-substrate methanol. The substrate conversions into the two products (2R,3R)-butane-2,3-diol and meso-butane-2,3-diol obtained after 16 h reaction time are shown in Figure 4A. Performing the BDH1-catalyzed acetoin reduction with the wild type strain P. pastoris CBS7435 resulted in an average conversion of ~5% (40 individual clones tested). Employing the single knock-out strains Δdas1 and Δdas2 in the same reaction did not yield substantially higher conversions. The average conversions were in the same order of magnitude as for the wild type strain (~6% and ~7% for the Δdas1 and Δdas2 strain, respectively), indicating that the NADH regeneration was not significantly improved in these strains. In contrast to the single knock-out strains, the acetoin conversion was 5.5-fold higher when using the double knock-out strain in comparison to the wild type (average conversion ~29%), indicating a more efficient cofactor supply. The higher conversions with the double-knock out strain were even obtained with fewer cells per reaction as it grew much slower on methanol than the wild type and the single knock-out strains. These first findings confirm the assumption that the NADH formation via methanol oxidation is increased when the assimilatory pathway is disrupted, if there is a NADH requirement in the cells due to, e.g., a biocatalytic reaction. The latter is only efficiently realized when both genes coding for the dihydroxyacetone synthase proteins are deleted.

[1860-5397-11-190-4]

Figure 4: BDH1-based whole-cell conversions of rac-acetoin. (A) Conversions of 25 mM rac-acetoin in the different knock-out strains were performed in 96 well deep-well plates for 16 h. The shown conversions represent mean values ± standard deviations derived from reactions using whole cells from 40 individual BDH1 transformants. (B) Time-resolved biotransformations of 50 mM substrate were conducted in the wild type (grey squares) and in the Δdas1 Δdas2 strain background (white squares). Background activity by endogenous acetoin reducing enzymes of P. pastoris was observed (grey triangles: P. pastoris CSB7435 wild type, white triangles: P. pastoris Δdas1 Δdas2).

The time course of acetoin conversions with representing BDH1 transformants in the wild type and Δdas1 Δdas2 background were investigated under optimized conditions in shake flasks. To avoid differences in the amount of cells employed in the biotransformation and to obtain higher product yields, cells corresponding to 3000 OD600 units were harvested 12 h after the first methanol induction and resuspended in 50 mL of buffered minimal medium before the conversions were started by the addition of substrate. During the first two hours of the whole-cell biotransformation, the conversions obtained with each of the strains were in the same order of magnitude (see Figure 4B). After longer reaction times, hardly any residual BDH1 activity was observed with the wild type strain (final conversion of ~50%), while the reaction reached 100% conversion after 6 h in the engineered strain. These findings clearly indicate that the NADH supply for the oxidoreductase can be attained over a prolonged reaction time in the P. pastoris Δdas1 Δdas2 strain, which directly translates into increased yields in the whole-cell reactions.

It has to be noted, that an additional acetoin reduction by endogenous Pichia dehydrogenases was also observed for the wild type and the double knock-out strain without the BDH1 expression cassette, reaching ~35% and ~8% substrate conversion, respectively. As for the recombinant strains, two products were detected, namely (2R,3R)-butane-2,3-diol and meso-butane-2,3-diol.

Conclusion

Efficient cofactor recycling is not only required for an optimal enzyme performance, but is also crucial to render the resulting process economical and sustainable. For this purpose, biotransformations based on whole cells represent an elegant strategy as the cell metabolism can be exploited for cofactor supply. We have generated a novel platform strain for whole-cell catalysis based on the methylotrophic yeast P. pastoris by engineering its methanol utilization pathway. By deleting the pathway for methanol assimilation, we forced flux through the dissimilatory pathway in which theoretically two molecules of NADH can be formed per molecule of methanol. The resulting double knock-out strain P. pastoris CBS7435 Δdas1Δdas2 displayed better performance in dehydrogenase based whole-cell biotransformations without the need of an external electron source. Higher conversions were achieved in comparison to reactions carried out with the wild type Pichia strain due to an extended NADH supply by the oxidation of methanol.

Methanol, which is a cheap carbon source, fulfills several roles in the presented biotransformations: It acts as an inducer of the PAOX1 regulated production of the redox enzyme as well as of the endogenous NADH regeneration system at the same time. The cofactor regeneration itself is based on methanol as co-substrate: the oxidation of methanol is irreversible and represents a strong thermodynamic driving force while only CO2 is produced as side product. Furthermore, methanol can serve as solvent for the substrate and methylotrophic yeasts are already naturally adapted to elevated concentrations of methanol.

The redesigned Pichia strain, thus, represents a valuable host for whole-cell applications where NADH regeneration is an issue. No additional over-expression of cofactor regenerating enzymes such as formate dehydrogenase, which only yields one molecule of NADH per carbon atom, is required. Due to its simplicity it might further boost the use of recombinant whole-cell catalysts in chemical and pharmaceutical industry.

Experimental

General

Unless stated otherwise, all chemicals were obtained from Sigma-Aldrich (Steinheim, Germany) or Carl-Roth (Karlsruhe, Germany) with the highest purity available. ZeocinTM was obtained from InvivoGen (San Diego, CA, USA). Phusion® High Fidelity Polymerase for DNA amplification and further DNA modifying enzymes were purchased from Thermo Fisher Scientific Inc. (Waltham, MA, USA). E. coli Top10 (Invitrogen, Carlsbad, USA) was used for all cloning steps and plasmid propagation. The P. pastoris strain CBS7435 as well as the plasmid pPp_T4_S were obtained from the Pichia pool of TU Graz [20].

Generation of das knock-out strains

The generation of knock-out strains was based on linear excision cassettes harboring a FLP recombinase system for inducible marker recycling. A schematic representation of such a knock-out cassette is provided in Supporting Information File 1, Figure S1. Knock-out cassettes were essentially constructed as described in [20]. Locus specific integration sequences, i.e., DNA fragments of approximately 1.5 kb directly located up- and downstream of the corresponding coding sequences, were amplified from genomic DNA. The corresponding primers were designed based on the genome sequence of P. pastoris CBS7435 and are summarized in Supporting Information File 1, Table S1. The resulting knock-out cassettes were employed for the transformation of P. pastoris CBS7435 wild type cells according to the condensed protocol by Lin-Cereghino et al. [23]. Transformants were selected on YPD agar plates containing 100 mg/L ZeocinTM. The correct integration of the knock-out cassette was confirmed by PCR using genomic DNA as template and primer pairs binding within the cassette and either up- or downstream of the targeted locus (see Supporting Information File 1, Table S2). In a next step, the marker was recycled by inducing the FLP recombinase. Therefore, a single colony from a correct knock-out strain was used to inoculate 50 mL of YPD media (250 mL baffled shake flask) and grown for 24 h at 28 °C. After 24 h of growth, methanol was added to a final concentration of 0.5% to start recombinant protein production, which was maintained by daily methanol addition for 96 h. An aliquot of these cultures was plated on YPD agar plates to obtain single colonies. These were subsequently streaked out on YPD agar plates supplemented with 100 mg/L ZeocinTM to identify clones that had excised the cassette and, thus, were ZeocinTM-sensitive. The marker recycling was further validated by PCR using primers that bind in the genomic region directly up- and downstream of the deleted locus (see Supporting Information File 1, Table S3) and Sanger sequencing of the resulting PCR product.

Growth rate studies

Liquid Pichia cultures were grown in buffered minimal medium containing 200 mM KPi (pH 6.0), 13.4 g/L yeast nitrogen base and 0.4 mg/L biotin supplemented either with 2% (w/v) D-glucose (BMD), 1% (w/v) glycerol (BMG) or 0.5% (v/v) methanol (BMM). Growth rates of the generated das knock-out strains were determined by measuring the optical density (OD600) of cultures in biological triplicate during the exponential growth phase.

GFP expression in knock-out strains

The plasmid pPp_T4_S_GFP was linearized with SmiI and used to transform the wild-type as well as the das knock-out P. pastoris strains. Single colonies were transferred to 96 well deep-well plates for standard cultivation and protein production as described previously [24]. For comparison of the expression levels, the GFP fluorescence (488 nm excitation, 507 nm emission) and the optical density (OD600) of the cell suspension were measured with a Synergy MX Microplate Reader.

Cloning of model enzyme

To evaluate the cofactor regeneration of the generated knock-out strains, the 2,3-butanediol dehydrogenase of S. cerevisiae YAL060W (BDH1) [22] was employed as NADH-dependent model enzyme. The corresponding gene was ligated with the P. pastoris expression vector pPp_T4_S_after digestion with EcoRI/NotI. The thus resulting construct, pPp_T4_S_BDH1, was linearized with SmiI for the subsequent transformation of the Pichia wild-type as well as das knock-out strains.

Screening of BDH1 transformants

Strains harboring the expression cassette for BDH1 were grown for 60 h in 250 µL of BMD medium in 96 well deep-well plates. Protein expression was started by the addition of 250 µL BMM2 (1% (v/v) in methanol) approximately 12 h prior to the start of the bioreduction reaction. The BDH1-mediated bioreduction was started by adding BMM10 (5% (v/v) methanol) containing 250 mM rac-acetoin. After a reaction time of 16 h, 300 µL of the reaction supernatant were extracted twice with 400 µL ethyl acetate containing 50 mM n-butanol as internal standard for the determination of acetoin conversions. The combined organic phases were dried over Na2SO4 and subjected to GC-FID analyses as described below.

Kinetic studies of biotransformations

Biotransformations in shake flasks were conducted with strains harboring one copy of the BDH1 expression cassette as determined by quantitative real-time PCR [25]. The corresponding strains were grown for 60 h in 200 mL BMD medium (2 L baffled shake flasks) and protein expression was started by the addition of 20 mL BMM10 approximately 12 h prior to the start of the bioreduction reaction. For BDH1 catalyzed acetoin conversion, cells corresponding to 3000 OD600 units were harvested by centrifugation (3000g, 10 min, rt) and resuspended in 50 mL of buffered minimal medium. The reaction was started by adding 10 mL of the substrate solution (300 mM rac-acetoin, 50% (v/v) methanol, 200 mM KPi, pH 6.0).

GC-FID analysis of biotransformations

Acetoin conversions were determined using an Agilent Technologies 6890N gas chromatograph equipped with an FID detector and a CTC Analytics CombiPAL autosampler. A Chirasil-DEX CB column (25 m × 0.32 mm, 0.25 µm film) was applied using H2 as carrier gas. The samples were injected without split. The following temperature program was used: 65 °C for 6.5 min; 50 °C/min to 80 °C; 80 °C for 0.7 min; 2 °C/min to 85 °C; 85 °C for 3 min.

Retention times: n-butanol: 1.71 min, (S)-acetoin: 2.04 min, (R)-acetoin: 2.32 min, (2R,3R)-butane-2,3-diol: 8.27 min, meso-butane-2,3-diol: 8.90 min.

Supporting Information

Supporting Information File 1: Schematic representation of knock-out cassette architecture and sequences of primers used.
Format: PDF Size: 102.0 KB Download

Acknowledgements

We gratefully acknowledge the help of Mudassar Ahmad in designing the employed knock-out cassettes. We further want to thank Thomas Vogl (TU Graz, Austria) for providing the plasmid harboring the coding sequence of GFP under the control of the AOX1 promoter.

The research leading to these results has received funding from the Innovative Medicines Initiative Joint Undertaking project CHEM21 under grant agreement n°115360, resources of which are composed of financial contribution from the European Union’s Seventh Framework Programme (FP7/2007-2013) and EFPIA companies’ in kind contribution. In addition, the work has been supported by the Federal Ministry of Science, Research and Economy (BMWFW), the Federal Ministry of Traffic, Innovation and Technology (bmvit), the Styrian Business Promotion Agency SFG, the Standortagentur Tirol, the Government of Lower Austria and ZIT - Technology Agency of the City of Vienna through the COMET-Funding Program managed by the Austrian Research Promotion Agency FFG.

References

  1. Johanson, T.; Katz, M.; Gorwa-Grauslund, M. F. FEMS Yeast Res. 2005, 5, 513–525. doi:10.1016/j.femsyr.2004.12.006
    Return to citation in text: [1] [2]
  2. Winkler, C.; Tasnádi, G.; Clay, D.; Hall, M.; Faber, K. J. Biotechnol. 2012, 162, 381–389. doi:10.1016/j.jbiotec.2012.03.023
    Return to citation in text: [1]
  3. Weckbecker, A.; Gröger, H.; Hummel, W. Regeneration of Nicotinamide Coenzymes: Principles and Applications for the Synthesis of Chiral Compounds. In Biosystems Engineering I; Wittmann, C.; Krull, R., Eds.; Advances in Biochemical Engineering / Biotechnology, Vol. 120; Springer: Berlin, Germany, 2010; pp 195–242. doi:10.1007/10_2009_55
    Return to citation in text: [1]
  4. Duetz, W. A.; Beilen, J. B.; Van Witholt, B. Curr. Opin. Biotechnol. 2001, 12, 419–425. doi:10.1016/S0958-1669(00)00237-8
    Return to citation in text: [1]
  5. Katz, M.; Sarvary, I.; Frejd, T.; Hahn-Hägerdal, B.; Gorwa-Grauslund, M. F. Appl. Microbiol. Biotechnol. 2002, 59, 641–648. doi:10.1007/s00253-002-1079-4
    Return to citation in text: [1]
  6. Baerends, R. J. S.; De Hulster, E.; Geertman, J.-M. A.; Daran, J.-M.; van Maris, A. J. A.; Veenhuis, M.; van der Klei, I. J.; Pronk, J. T. Appl. Environ. Microbiol. 2008, 74, 3182–3188. doi:10.1128/AEM.02858-07
    Return to citation in text: [1]
  7. Schroer, K.; Luef, K. P.; Hartner, S. F.; Glieder, A.; Pscheidt, B. Metab. Eng. 2010, 12, 8–17. doi:10.1016/j.ymben.2009.08.006
    Return to citation in text: [1] [2]
  8. Cregg, J. M.; Cereghino, J. L.; Shi, J.; Higgins, D. R. Mol. Biotechnol. 2000, 16, 23–52. doi:10.1385/MB:16:1:23
    Return to citation in text: [1]
  9. Ahmad, M.; Hirz, M.; Pichler, H.; Schwab, H. Appl. Microbiol. Biotechnol. 2014, 98, 5301–5317. doi:10.1007/s00253-014-5732-5
    Return to citation in text: [1]
  10. Engelking, H.; Pfaller, R.; Wich, G.; Weuster-Botz, D. Tetrahedron: Asymmetry 2004, 15, 3591–3593. doi:10.1016/j.tetasy.2004.09.021
    Return to citation in text: [1]
  11. Das, S.; Glenn, J. H., IV; Subramanian, M. Biotechnol. Prog. 2010, 26, 607–615. doi:10.1002/btpr.363
    Return to citation in text: [1]
  12. Abad, S.; Nahalka, J.; Bergler, G.; Arnold, S. A.; Speight, R.; Fotheringham, I.; Nidetzky, B.; Glieder, A. Microb. Cell Fact. 2010, 9, 24. doi:10.1186/1475-2859-9-24
    Return to citation in text: [1]
  13. Geier, M.; Braun, A.; Emmerstorfer, A.; Pichler, H.; Glieder, A. Biotechnol. J. 2012, 7, 1346–1358. doi:10.1002/biot.201200187
    Return to citation in text: [1]
  14. Yan, J.; Zheng, X.; Li, S. Bioresour. Technol. 2014, 151, 43–48. doi:10.1016/j.biortech.2013.10.037
    Return to citation in text: [1]
  15. Wriessnegger, T.; Augustin, P.; Engleder, M.; Leitner, E.; Müller, M.; Kaluzna, I.; Schürmann, M.; Mink, D.; Zellnig, G.; Schwab, H.; Pichler, H. Metab. Eng. 2014, 24, 18–29. doi:10.1016/j.ymben.2014.04.001
    Return to citation in text: [1]
  16. Hartner, F. S.; Glieder, A. Microb. Cell Fact. 2006, 5, 39. doi:10.1186/1475-2859-5-39
    Return to citation in text: [1]
  17. De Schutter, K.; Lin, Y.-C.; Tiels, P.; Van Hecke, A.; Glinka, S.; Weber-Lehmann, J.; Rouzé, P.; Van de Peer, Y.; Callewaert, N. Nat. Biotechnol. 2009, 27, 561–566. doi:10.1038/nbt.1544
    Return to citation in text: [1]
  18. Krainer, F. W.; Dietzsch, C.; Hajek, T.; Herwig, C.; Spadiut, O.; Glieder, A. Microb. Cell Fact. 2012, 11, 22. doi:10.1186/1475-2859-11-22
    Return to citation in text: [1]
  19. Reuß, O.; Vik, A.; Kolter, R.; Morschhäuser, J. Gene 2004, 341, 119–127. doi:10.1016/j.gene.2004.06.021
    Return to citation in text: [1]
  20. Näätsaari, L.; Mistlberger, B.; Ruth, C.; Hajek, T.; Hartner, F.; Glieder, A. PLoS One 2012, 7, e39720. doi:10.1371/journal.pone.0039720
    Return to citation in text: [1] [2] [3]
  21. Broach, J. R.; Guarascio, V. R.; Jayaram, M. Cell 1982, 29, 227–234. doi:10.1016/0092-8674(82)90107-6
    Return to citation in text: [1]
  22. González, E.; Fernández, M. R.; Larroy, C.; Solà, L.; Pericàs, M. A.; Parés, X.; Biosca, J. A. J. Biol. Chem. 2000, 275, 35876–35885. doi:10.1074/jbc.M003035200
    Return to citation in text: [1] [2]
  23. Lin-Cereghino, J.; Wong, W. W.; Xiong, S.; Giang, W.; Luong, L. T.; Vu, J.; Johnson, S. D.; Lin-Cereghino, G. P. BioTechniques 2005, 38, 44–48. doi:10.2144/05381BM04
    Return to citation in text: [1]
  24. Weis, R.; Luiten, R.; Skranc, W.; Schwab, H.; Wubbolts, M.; Glieder, A. FEMS Yeast Res. 2004, 5, 179–189. doi:10.1016/j.femsyr.2004.06.016
    Return to citation in text: [1]
  25. Abad, S.; Kitz, K.; Hörmann, A.; Schreiner, U.; Hartner, F. S.; Glieder, A. Biotechnol. J. 2010, 5, 413–420. doi:10.1002/biot.200900233
    Return to citation in text: [1]

© 2015 Geier et al; licensee Beilstein-Institut.
This is an Open Access article under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/2.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.
The license is subject to the Beilstein Journal of Organic Chemistry terms and conditions: (http://www.beilstein-journals.org/bjoc)

 
Back to Article List