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PLoS One. 2009; 4(12): e8317.
Published online 2009 Dec 15. doi:  10.1371/journal.pone.0008317
PMCID: PMC2789386

An Engineered Yeast Efficiently Secreting Penicillin

Paulo Lee Ho, Editor


This study aimed at developing an alternative host for the production of penicillin (PEN). As yet, the industrial production of this β-lactam antibiotic is confined to the filamentous fungus Penicillium chrysogenum. As such, the yeast Hansenula polymorpha, a recognized producer of pharmaceuticals, represents an attractive alternative. Introduction of the P. chrysogenum gene encoding the non-ribosomal peptide synthetase (NRPS) δ-(L-α-aminoadipyl)-L-cysteinyl-D-valine synthetase (ACVS) in H. polymorpha, resulted in the production of active ACVS enzyme, when co-expressed with the Bacillus subtilis sfp gene encoding a phosphopantetheinyl transferase that activated ACVS. This represents the first example of the functional expression of a non-ribosomal peptide synthetase in yeast. Co-expression with the P. chrysogenum genes encoding the cytosolic enzyme isopenicillin N synthase as well as the two peroxisomal enzymes isopenicillin N acyl transferase (IAT) and phenylacetyl CoA ligase (PCL) resulted in production of biologically active PEN, which was efficiently secreted. The amount of secreted PEN was similar to that produced by the original P. chrysogenum NRRL1951 strain (approx. 1 mg/L). PEN production was decreased over two-fold in a yeast strain lacking peroxisomes, indicating that the peroxisomal localization of IAT and PCL is important for efficient PEN production. The breakthroughs of this work enable exploration of new yeast-based cell factories for the production of (novel) β-lactam antibiotics as well as other natural and semi-synthetic peptides (e.g. immunosuppressive and cytostatic agents), whose production involves NRPS's.


β-Lactam antibiotics (penicillins and cephalosporins) represent a class of important drugs of major clinical value. Their significant economical value is evident from the fact that β-lactam antibiotics contribute to over 40% of the total antibiotic market [1]. The industrial production of penicillin (PEN) occurs via fermentation using the filamentous fungus Penicillium chrysogenum. There is considerable interest in developing novel cell factories for the production of (new) β-lactam antibiotics, because of the intrinsic drawbacks of filamentous fungi for large scale industrial fermentations. Unicellular yeast species are very attractive alternatives as they have superior fermentation characteristics over filamentous fungi. Production of PEN and other β-lactam antibiotics in yeast will also provide new opportunities for highly sustainable production processes and the development of generic strategies to produce modified β-lactams and eventually other peptide antibiotics using the power of yeast genetics.

The yeast Hansenula polymorpha, a recognized producer of pharmaceuticals [2], represents an attractive alternative for PEN production. Advantages of this organism include the availability of very strong and regulatable promoters and excellent fermentation properties. An example includes the large scale industrial production of hepatitis B antigen [2]. Also, in this yeast peroxisomes can be massively induced. This is a favorable property to facilitate PEN production, which is known to involve peroxisomal enzymes.

Adapting yeast to produce PEN requires the introduction of the complete PEN biosynthetic pathway in the organism. This involves the non-ribosomal peptide synthetase (NRPS) δ-(L-α-aminoadipyl)-L-cysteinyl-D-valine synthetase (ACVS), isopenicillin N synthase (IPNS), isopenicillin N acyl transferase (IAT) and phenylacetyl CoA ligase (PCL). Of these, ACVS and IPNS are cytosolic, whereas IAT and PCL are localized to peroxisomes (Fig. 1) [3]. Notably, ACVS belongs to a class of enzymes (NRPS's) that exclusively occurs in certain filamentous fungi and bacteria (Actinomycetes, Bacilli).

Figure 1
Schematic representation of the penicillin G (PenG) biosynthetic pathway in P. chrysogenum.

Here we show that we successfully engineered H. polymorpha to produce biologically active PEN. Our work involves major breakthroughs by showing:

  1. the functional expression of an NRPS in yeast,
  2. the successful reconstitution of the complete, compartmentalized PEN biosynthetic pathway in H. polymorpha
  3. that PEN is highly efficiently secreted by H. polymorpha.
  4. that the peroxisomal localization of the last two enzymes of the PEN biosynthesis pathway is important for efficient PEN production.

These achievements are of major significance for the development of novel yeast-based production platforms for the production of novel β-lactams and other important peptide-based pharmaceuticals.


Functional Production of ACVS in H. polymorpha

In our approach to reprogram H. polymorpha to produce PEN, we first set out to generate a strain synthesizing enzymatically active ACVS, a 450 kD NRPS. Upon introduction of the P. chrysogenum pcbAB gene encoding ACVS in H. polymorpha (strain HpPen1), the protein was properly produced and localized to the cytosol (Fig. 2 and and3).3). However, when these cells were grown in the presence of the ACVS substrate α-aminoadipic acid (AAA), ACV production could not be demonstrated (Fig. 4). This was most likely related to the fact that activation of NRPS enzymes requires covalent attachment of a phosphopantetheinyl moiety to the peptidyl carrier protein domain of the enzyme [4], a reaction that is catalyzed by phosphopantetheinyl transferases (PPTases). Apparently, H. polymorpha does not contain a PPTase that is able to activate ACVS in vivo. Therefore, we introduced the Bacillus subtilis PPTase Sfp, which exhibits a broad substrate specificity [5], in HpPen1, thus generating strain HpPen2 (Fig. 3).

Figure 2
Subcellular localization of ACVS in H. polymorpha.
Figure 3
Expression of genes involved in penicillin G production in H. polymorpha.
Figure 4
ACV production in HpPen2.

When HpPen2 was grown in the presence of AAA, ACV was indeed produced (Fig. 4), demonstrating that B. subtilis Sfp had activated ACVS. ACV was not observed when HpPen2 cells were grown in the absence of AAA (Fig. 4), which indicates that AAA is a limiting substrate in H. polymorpha, but can be taken up by the yeast cells from the cultivation medium.

Secretion of a Bioactive β-Lactam by H. polymorpha

Subsequently, we introduced P. chrysogenum IPNS in HpPen2 to produce IPN, the next intermediate of the PEN biosynthesis pathway [6] (Fig. 1). In the resulting strain (HpPen3), ACVS, Sfp and IPNS were properly produced (Fig. 3). Upon growth of these cells in medium containing AAA, intracellular accumulation of a β-lactam antibiotic (presumably IPN) could be demonstrated in a bioassay using the β-lactam sensitive indicator strain Micrococcus luteus [7] (Fig. 5A). Growth of this indicator strain was not inhibited when an extract was used of similarly grown HpPen2 control cells (Fig. 5A). The presence of enzymatically active ACVS and IPNS in cells of strain HpPen3 to form IPN was confirmed using an in vitro assay (Fig. 5B).

Figure 5
Production of β-lactam antibiotics in H. polymorpha.

PEN Production in Yeast

As a final step to produce PEN in H. polymorpha, we introduced the genes that encode the P. chrysogenum peroxisomal enzymes IAT and PCL in HpPen3, resulting in strain HpPen4 (Fig. 3). We previously showed that both heterologous proteins are properly synthesized and sorted in H. polymorpha [8], [9]. To test whether HpPen4 cells produced and secreted the β-lactam antibiotic penicillin G (PenG), cells were grown in media supplemented with AAA and phenylacetic acid (PAA), the PenG side chain precursor. As shown in Fig. 5C (extracellular), a clear zone of growth inhibition of M. luteus was observed in the bioassay using spent medium of the HpPen4 culture. Growth inhibition was not observed when medium of a control HpPen3 culture was used. This data suggests that PenG is produced and secreted by HpPen4 cells.

LC-MS/MS analyses of spent medium of the HpPen4 culture confirmed the presence of compounds that have the same accurate masses as PenG and IPN (Fig. 6). Furthermore, MS/MS fragmentation patterns of these substances were identical to those obtained using pure IPN or PenG (Fig. 6).

Figure 6
H. polymorpha cells produce and secrete PenG: LC MS/MS demonstration of PEN production.

Interestingly, using the same volume of spent media of cultures of P. chrysogenum NRRL1951 and HpPen4 halo's of similar size were obtained in the bioassay (Fig. 5C). P. chrysogenum NRRL1951 is the strain from which all subsequent high producing strains are derived.

Halo's were also observed when crude extracts were used of HpPen3 or HpPen4 cells, which had been grown in the presence of AAA and PAA (Fig. 5C intracellular). However, extracts corresponding to large culture volumes (100 times more than of the spent medium) had to be used to obtain these halo's (Fig. 5C). In HpPen3 cell extracts the halo is most likely due to the accumulation of IPN, whereas for HpPen4 cells residual amounts of PenG and IPN may remain inside the cells.

PEN Is Efficiently Secreted by HpPen4 Cells

Subsequent detailed quantitative analysis of IPN and PenG using ion-pair reversed-phase liquid chromatography–electrospray ionization isotope dilution tandem mass spectrometry (IP-LC–ESI-ID-MS/MS) confirmed that IPN indeed accumulates inside HpPen3 cells (Fig. 7). In identically grown HpPen4 cultures the level of intracellular IPN was reduced relative to those in HpPen3 cells. However, these cells produced PenG, which was predominantly present extracellularly, confirming that PenG is secreted by HpPen4 cells. Calculation of the intracellular metabolite concentrations revealed that PenG is efficiently secreted by HpPen4 cells (the ratio of the extracellular/intracellular concentration of PenG is 24). However, how PenG and its intermediates are transported over the peroxisome and plasma membrane is still largely speculative. Recently, the presence of a regulatable porin in the peroxisomal membrane has been described [10] that could be involved in this process. The HpPen4 cells also produced low concentrations of 6-amino penicillinic acid (6-APA), which was barely detectable in HpPen3. In HpPen4 cells 6-APA is most likely formed by hydrolysis of IPN [11]. In line with the analyses shown in Fig. 6, IPN was also detectable in the medium of HpPen4 cultures. The amount however was too low to allow accurate quantification using the IP-LC–ESI-ID-MS/MS method used.

Figure 7
Quantification of produced β-lactam compounds in HpPen3 and HpPen4 cultures.

Peroxisomes Are Important for Efficient PEN Production

To analyse the importance of the peroxisome compartment in PEN-producing H. polymorpha cells, we analyzed PenG production in HpPen4 cells in which the PEX3 gene was deleted (Δpex3 HpPen4).

Cells were grown on glucose/choline to allow PAOX induction, as Δpex3 HpPen4 cells can not grow on methanol. Deletion of PEX3 in H. polymorpha results in the complete absence of recognizable peroxisomal structures and the mislocalization of all peroxisomal enzymes to the cytosol [12]. Bioassays revealed that a significantly smaller halo was formed using medium of the Δpex3 HpPen4 culture relative to HpPen4 medium (Fig. 8). This was confirmed by MS/MS data, which indicated that in glucose/choline grown cells the PenG production had decreased over 50% (1.1 µg/ml in HpPen4 vs 0.4 µg/ml in Δpex3 HpPen4). Hence, compartmentalization of IAT and PCL in peroxisomes is important for efficient PenG production in H. polymorpha.

Figure 8
Deletion of PEX3 results in reduced PEN secretion.


Here we present a proof of principle that cells of the yeast H. polymorpha can be engineered to produce the important β-lactam antibiotic PEN by introduction of four P. chrysogenum genes and one B. subtilis gene. This achievement includes several major breakthroughs. First, we show the functional expression of an NRPS in yeast. Secondly, we successfully reconstituted a complex, compartmentalized biosynthetic pathway in yeast that is catalyzed by cytosolic and peroxisomal enzymes and requires transport of precursors, intermediates and end products across the peroxisomal and plasma membrane (Fig. 1). Finally, we demonstrate that intact peroxisomes are required for efficient product formation.

Functional expression of the NRPS ACVS in H. polymorpha was dependent on the function of a heterologous PPTase, to modify the protein by covalent binding of phosphopantetheinyl moieties. Apparently, the endogenous H. polymorpha PPTase (Lys5) is unable to activate ACVS, whereas the broad specificity bacterial enzyme is suitable for this modification and functional in vivo in H. polymorpha. While this paper was under review [13] published a similar result, expressing functional ACVS in baker's yeast.

Functionally expression of an NRPS in yeast opens the way to explore novel and improved processes to produce other NRPS-based natural peptides in this cell factory. NRPS's allow synthesis of a broad range of valuable compounds, including almost all peptide-based antibiotics as well as other clinically important compounds such as immunosuppressors and anti-tumor compounds [14].

Our data open the way to use yeast as a host organism for NRPS engineering. NRPS engineering is a strongly emerging field [15], [16] with ample opportunities to develop novel products and processes. These developments rely on efficient NRPS production systems that have now become available in yeast. A single NRPS consist of an arrangement of modules, in which each module is responsible for the incorporation and modification of one amino acid building blocks in the growing polypeptide chain. This modular structure of NRPS's renders them highly attractive targets for protein engineering by domain swapping or active-site modifications. Taking advantage of the power of yeast genetics and handling, our finding offers important novel options that highly facilitate NRPS engineering.

In P. chrysogenum, PEN production is compartmentalized in peroxisomes and the cytosol. The efficient secretion of PEN produced in H. polymorpha indicates that highly dedicated P. chrysogenum transporter proteins apparently are not required for the intracellular transport processes, for uptake of PAA and AAA, nor for the efficient secretion of the end product. Also, compartmentalization is important for efficient PEN production, as the PEN production levels were reduced in a peroxisome deficient (Δpex3) background. In Aspergillus nidulans a relation between peroxisome function and PEN production was observed as well [17]. Why the peroxisomal localization of IAT and PCL is important, remains however obscure.

The current non-optimized H. polymorpha strain produces similar amounts of PEN as the original P. chrysogenum strain (NRRL1951). Future up-scaling programs will strongly benefit from the advanced molecular toolbox available for H. polymorpha [2], [18], [19] that is not yet available for P. chrysogenum. These approaches can also be used to rapidly develop novel antibiotics by introducing additional heterologous genes and high throughput screening procedures. The development of novel antibiotics is extremely important because of the continuous combat against antibiotic resistant bacteria. Because H. polymorpha grows well on various cheap carbon sources (e.g. methanol), the newly engineered cell factory also enables producing these components from alternative and sustainable feedstocks.

Materials and Methods

Microorganisms and Growth

The H. polymorpha strains used are derivatives of NCYC495 ade11.1 leu1.1 [20] and listed in Table 1. All plasmids are indicated in Table 2.

Table 1
H. polymorpha strains used in this study.
Table 2
Plasmids used in this study.

Yeast cells were grown at 25°C in batch cultures on 0.5% methanol for 36 hours [6] or in carbon-limited chemostat cultures [21], [22]. Chemostat cultures were grown at a dilution rate of 0.1 h−1, pH 5.0. The feed contained a mixture of glucose (0.25%) and methanol (0.2%) [22] or glucose (0.25%) and choline (0.2%) [21].

P. chrysogenum strains DS17690 [23] and NRRL1951 [24] were grown in batch cultures on a defined PEN production medium supplemented with 3 mM PAA [25]. Micrococcus luteus ATCC 9341 was used for bioassays and grown on 2 x YT agar plates containing 2% bacto-tryptone, 1% yeast extract and 1% NaCl at 30°C.

Construction of Plasmids

Plasmid pZ4-pcbAB

To facilitate cloning of the P. chrysogenum pcbAB gene, a HindIII site was introduced upstream of the start codon by PCR with the primers ACVS-forward (5′ AGAAAGCTTATGACTCAACTGAAGCCAAA-3′) and ACVS reverse (5′ CTTATCTAGAAACAATGCGAC 3′) using plasmid pME1213 as template. Subsequently, the resulting 1.1 kb product was cloned as a HindIII-XbaI fragment into the HindIII+XbaI-digested vector pHIPZ4. The resulting plasmid was digested with XbaI+SmaI and an XbaI-SmaI fragment of plasmid pME1213, containing the remainder of the pcbAB gene, was inserted. The resulting plasmid, designated pZ4-pcbAB, contains the entire P. chrysogenum pcbAB gene flanked by the inducible H. polymorpha alcohol oxidase promoter (PAOX) and the amine oxidase terminator (TAMO).

Plasmid pG4U-pcbAB

A 13,777 bp NotI-SmaI fragment of plasmid pZ4-pcbAB, containing the P. chrysogenum pcbAB gene and the H. polymorpha PAOX region, was inserted into SalI (blunted by Klenow treatment) + NotI-digested plasmid pHIPG4U. The resulting plasmid, designated pG4U-pcbAB, contains the entire P. chrysogenum pcbAB gene flanked by the H. polymorpha PAOX and TAMO regulatory sequences, a dominant selection marker conferring resistance to G-418 and the H. polymorpha URA3 gene for targeted integration.

Plasmid pA7-Sfp.His6

We first amplified the B. subtilis sfp.His6 fusion gene with primers Sfp-F (5′ GCGGATCCATGAAGATTTACGGAATTTATATGG 3′) and Sfp-R (5′ TCGGTC GACTTAGTGATGGTGATGGTGATGAGATC 3′) using plasmid pQE60-Sfp.His6 as template. The resulting PCR product was then inserted as a BamHI-SalI fragment into BamHI+SalI-digested plasmid pHIPA4, resulting in plasmid pA4-Sfp.His6. In order to have constitutive expression of the sfp.His6 gene, the H. polymorpha PAOX region of pA4-Sfp.His6 (flanked by NotI and BamHI sites) was replaced by a NotI-BamHI fragment containing the H. polymorpha TEF1 promoter of pHIPX7. The resulting plasmid, pA7-Sfp.His6, contains the B. subtilis sfp.His6 gene flanked by the H. polymorpha PTEF1 and TAMO regulatory sequences and the H. polymorpha ADE11 gene as auxotrophic marker.


First, we isolated the blasticidine gene from plasmid pPIC6-A as a 1969 bp BamHI (blunted by Klenow treatment)-BglII fragment and cloned that between the SpeI (blunted by Klenow treatment) and BglII sites of plasmid pHP-penDE resulting in plasmid pB4-IAT. In order to clone the pclA gene encoding P. chrysogenum phenylacetyl CoA ligase in plasmid pB4-IAT, plasmid pHIPM4-PCLSKL was digested with Spe1 and the resulting 6146 bp fragment was ligated into XbaI-linearized pB4-IAT, resulting in plasmid pBM4-IAT.PCLSKL. In this plasmid the P. chrysogenum penDE and pclASKL genes are both controlled by H. polymorpha PAOX and TAMO regulatory sequences.

Construction of H. polymorpha Strains

HpPen1 and HpPen2

A H. polymorpha strain producing ACVS (strain HpPen1) was constructed as follows: Plasmid pG4U-pcbAB was linearized with Bst1107I in the H. polymorpha URA3 region and transformed into H. polymorpha NCYC495 ade11.1 leu1.1 ura3 met6. Uracil-prototrophic transformants were selected and also tested for G-418 resistance (50 µg/ml). A strain producing ACVS was designated HpPen1.

Strain HpPen2 was generated by integration of NdeI-linearized plasmid pA7-Sfp.His6 in the genome of HpPen1 with selection on adenine prototrophy and production of both ACVS and Sfp.His6.

HpPen3 and HpPen4

For the purpose of generating an H. polymorpha strain expressing all PEN biosynthesis genes, plasmid pZ4-pcbAB was digested with SspI and used to transform the H. polymorpha strain HpIPNS #4.2. Transformants were selected on YPD plates that contained zeocin (300 µg/ml). A strain producing both ACVS and IPNS was designated HpIPNS.ACVS. For construction of HpPen3, plasmid pA7-Sfp.His6 was digested with NotI and KpnI and the resulting 4656 bp DNA fragment was used to transform strain HpIPNS.ACVS. Adenine prototrophic transformants were selected. A transformant that produced ACVS, Sfp.His6 and IPNS was designated HpPen3.

For the purpose of stable integration of the P. chrysogenum pcbDE and pclASKL genes, plasmid pBM4-IAT.PCLSKL was linerarized using NdeI in the MET6 locus. The linerarized plasmid was then transfomed into strain HpPen3. Transformants were selected on YPD plates with blasticidine (300 µg/ml). A strain producing all five PEN enzymes was designated HpPen4.


In order to create a peroxisome deficient derivative of HpPen4, the pex3::nat deletion cassette was PCR amplified from plasmid pSNA04 with primers pex3-nat-fw ( 5′ ACCGCGTGAAACTTTATATCG 3′) and pex3-nat-rev (5′ CAAGGAACGCGATGTATGTT 3′). The resulting 1923 bp fragment was used to transform HpPen4. Transformants were selected on YPD plates with nourseothricin (100 µg/ml). Correct deletion of PEX3 was confirmed using Southern blot analysis. The resulting strain was designated Δpex3.HpPen4.

Biochemical Methods

Crude extracts of H. polymorpha cells [26] and P. chrysogenum hyphae [27] were prepared as described previously. Protein concentrations were determined using the Bio-Rad Protein Assay system using bovine serum albumin as a standard. Western blots were prepared using extracts of H. polymorpha and P. chrysogenum cells, obtained using the TCA method [27], and decorated using antibodies raised against IPNS, ACVS, IAT, PCL [8], [28], or the His6 tag (Santa Cruz Biotechnology, INC.).


The presence of β-lactams was analysed by a bioassay using agar plates on which M. luteus cells were plated. Samples were loaded in wells in the plates and growth was monitored upon overnight incubation at 30°C. To detect the formation of β-lactams in vitro, crude extracts were prepared in buffer A containing 100 mM Tris-HCl pH 8.0, 20% glycerol, 2 mM DTT, 25 mM KCl and 1 mM PMSF. Small molecules were removed from P. chrysogenum crude extracts by gel filtration using a PD-10 column. Extracts were incubated at 25°C in buffer A supplemented with 5 mM AAA, 1 mM L-cysteine, 5 mM L-valine, 5 mM ATP, 20 mM MgCl2, 0.43 mM FeSO4. 7H2O and 14.1 mM L-ascorbic acid. After 60 min of incubation, the reaction was terminated by addition of 5 mM of EDTA pH 8.0. The presence of β-lactams was monitored using the bioassay as detailed above. As a control, samples were incubated with β-lactamase (50,000 IU per reaction) prior to termination of the reaction.

Detection of Metabolites

10 ml of chemostat broth was sampled directly into a filtration beaker containing 50 ml of a −40°C 60% v/v aqueous methanol quenching solution. The quenched cells were filtered over a glass fiber filter (type A/E, Pall Corporation, East Hills, NY, USA, 47 mm diameter, 1 µm pore size) and was washed with 2×50 ml of the quenching solution to completely remove extracellular metabolites. For accurate quantification purposes by IDMS [29] 100 µl of 13C internal standard solution was added to the cells. This 13C internal standard solution contained all relevant metabolites as U-13C-labeled isotopes. Immediately after the cells were submerged in a tube containing 30 ml of a 73°C 75% v/v aqueous ethanol solution. The tube was vigorously mixed and transferred to a water bath at 95°C for 5 min for extraction of metabolites and inactivation of enzymes. The extract was concentrated under vacuum and analysed via ion-pair reversed-phase liquid chromatography-isotope dilution tandem mass spectrometry (IP-LC-ESI-ID-MS/MS) as described previously [30]. The same analysis method was used to determine extracellular metabolite concentrations in quenched and filtered chemostat broth, which was obtained as described previously [31]. The concentration of intracellular metabolites were calculated, assuming a cellular liquid content of 2.38 ml per g dry weight [32].

Mass Spectrometry Analysis of β-Lactams

For liquid chromatographical analysis, samples were separated on a C18 capillary column (Waters sunfire C18, 2.1×150 mm, 1.8 µm particle size LC column, Waters Chromatography B.V The Netherlands) coupled to an Accela pump (Thermo Electron Corporation). The injection volume was 25 µl, the flow rate 200 µl/min and the elution temperature 30°C. Gradients were prepared using solution A (20 mM ammonium formate in milli Q water) and solution B (a 1∶1 mixture of 20 mM ammonium formate in milli Q water and acetonitrile). A gradient of 5–50% solution B was ran during 12 min, followed by a gradient of 50–65% solution B during 3 min, a washing step with a gradient of 65–5% solution B during 3 min followed by regeneration of the column with 5% solution B. As controls, standard IPN (synthesized by Syncom B.V., the Netherlands) and PenG (Sigma Aldrich) solutions were analysed to determine their respective retention times. Following LC separation, the eluates were directly analysed by mass determination using an LTQ orbitrap (Thermo Electron Corporation). MS data acquisition was performed in positive ion mode. For structure determination MS/MS was performed using LTQ XL (Thermo Electron Corporation) with an m/z range of 200–1000.


We thank Olaf Schouten, DSM Biotechnology Center for the MS analysis.


Competing Interests: The authors have declared that no competing interests exist.

Funding: LG, JAKWK and RD are financially supported by the Netherlands Ministry of Economic Affairs and the B-Basic partner organizations (www.b-basic.nl) through B-Basic, a public-private NWO-ACTS programme (ACTS  =  Advanced Chemical Technologies for Sustainability). This project was carried out within the research programme of the Kluyver Centre for Genomics of Industrial Fermentation, which is part of the Netherlands Genomics Initiative/Netherlands Organization for Scientific Research. The funders had no role in study design, data collection and analysis, decision to publish, or preparation of the manuscript.


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