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. 2019 Apr 10;9:e00090. doi: 10.1016/j.mec.2019.e00090

Alone at last! – Heterologous expression of a single gene is sufficient for establishing the five-step Weimberg pathway in Corynebacterium glutamicum

Christian Brüsseler 1, Anja Späth 1, Sascha Sokolowsky 1, Jan Marienhagen 1,∗
PMCID: PMC6475665  PMID: 31016135

Abstract

Corynebacterium glutamicum can grow on d-xylose as sole carbon and energy source via the five-step Weimberg pathway when the pentacistronic xylXABCD operon from Caulobacter crescentus is heterologously expressed. More recently, it could be demonstrated that the C. glutamicum wild type accumulates the Weimberg pathway intermediate d-xylonate when cultivated in the presence of d-xylose. Reason for this is the activity of the endogenous dehydrogenase IolG, which can also oxidize d-xylose. This raised the question whether additional endogenous enzymes in C. glutamicum contribute to the catabolization of d-xylose via the Weimberg pathway. In this study, analysis of the C. glutamicum genome in combination with systematic reduction of the heterologous xylXABCD operon revealed that the hitherto unknown and endogenous dehydrogenase KsaD (Cg0535) can also oxidize α-ketoglutarate semialdehyde to the tricarboxylic acid cycle intermediate α-ketoglutarate, the final enzymatic step of the Weimberg pathway. Furthermore, heterologous expression of either xylX or xylD, encoding for the two dehydratases of the Weimberg pathway in C. crescentus, is sufficient for enabling C. glutamicum to grow on d-xylose as sole carbon and energy source. Finally, several variants for the carbon-efficient microbial production of α-ketoglutarate from d-xylose were constructed. In comparison to cultivation solely on d-glucose, the best strain accumulated up to 1.5-fold more α-ketoglutarate in d-xylose/d-glucose mixtures.

Keywords: Corynebacterium glutamicum, D-xylose, Weimberg pathway, α-ketoglutarate

Highlights

  • •

    C. glutamicum requires only one additional dehydratase to grow on d-xylose.

  • •

    XylX or XylD can be used to establish the Weimberg pathway in C. glutamicum.

  • •

    cg0535 (ksaD) encodes for an α-ketoglutarate semialdehyde dehydrogenase.

  • •

    C. glutamicum accumulates α-ketoglutarate from d-xylose via the Weimberg pathway.

1. Introduction

The Gram-positive bacterium Corynebacterium glutamicum has a long history in the industrial production of proteinogenic amino acids. In particular l-glutamate and l-lysine are produced at million ton-scale with this microorganism (Eggeling and Bott, 2015; Lee and Wendisch, 2017). Furthermore, C. glutamicum strains for more than 70 biotechnologically interesting compounds such as alcohols, organic acids or polyphenols have been engineered over the last years (Becker et al., 2018; Kallscheuer et al., 2016, 2017; Vogt et al., 2016; Wieschalka et al., 2013). However, all large-scale applications for amino acid production with C. glutamicum use d-glucose from starch hydrolysates or d-fructose (and sucrose) from molasses and the substrate spectrum of C. glutamicum variants engineered for other small molecules is also for the most part limited to these hexoses (Blombach and Seibold, 2010).

More recent studies focus on engineering C. glutamicum for the utilization of lignocellulose-derived pentoses d-xylose and l-arabinose as C. glutamicum cannot naturally catabolize these sugars (Kawaguchi et al., 2006, 2008). In case of d-xylose, two different metabolic routes have been individually added to the catabolic repertoire of C. glutamicum. In the Isomerase pathway, d-xylose is first converted to d-xylulose by a heterologous d-xylose isomerase (encoded by xylA from either Escherichia coli or Xanthomonas campestris) and subsequently phosphorylated by an endogenous d-xylulokinase (encoded by xylB) yielding d-xylulose-5-phosphate, which can be rapidly metabolized (Kawaguchi et al., 2006; Meiswinkel et al., 2013). Several C. glutamicum strains, capable of utilizing d-xylose via the Isomerase pathway have been engineered for the production of succinate, ethanol, lysine, glutamate, ornithine, putrescine and 1,5-diaminopentane (Buschke et al., 2011; Jo et al., 2017; Meiswinkel et al., 2013). In contrast, functional introduction of the xylXABCD operon from Caulobacter crescentus enabled C. glutamicum to grow on d-xylose as sole carbon and energy source via the five-step Weimberg pathway (Radek et al., 2014). In this pathway, d-xylose is initially oxidized to 1,4-d-xylonolactone via a xylose dehydrogenase (XylB) and subsequently hydrolyzed by a d-xylonolactonase (XylC) yielding d-xylonate (Fig. 1). Two subsequent dehydration reactions, catalyzed by a d-xylonate dehydratase (XylD) and a 2-keto-3-deoxyxylonate dehydratase (XylX), lead to α-ketoglutarate semialdehyde, which is finally oxidized by an α-ketoglutarate semialdehyde dehydrogenase (XylA) to the tricarboxylic acid (TCA)-cycle intermediate α-ketoglutarate. However, C. glutamicum WMB1 as the first engineered strain having the Weimberg pathway allowed only for a growth rate of μ = 0.07 h−1 on d-xylose containing defined medium. Adaptive laboratory evolution improved d-xylose utilization by 260 % yielding the strain C. glutamicum WMB2evo (μmax = 0.26 h−1) (Radek et al., 2017). Genome sequencing of this strain revealed a functional loss of the transcriptional regulator IolR, which controls the expression of 22 genes for the most part believed to be involved in myo-inositol metabolization (Klaffl et al., 2013). Among these genes is iolT1 encoding for the myo-inositol/proton symporter IolT1, which turned out to also contribute to d-xylose uptake in C. glutamicum (Brüsseler et al., 2018). By rationally introducing two point mutations into the IolR-binding site of the iolT1-promoter yielding C. glutamicum PO6 iolT1, this effect could be successfully mimicked. Furthermore, an endogenously encoded d-xylose dehydrogenase (IolG) contributing to the oxidation of d-xylose in C. glutamicum could be identified, which was subsequently employed for the carbon efficient production of d-xylonate with C. glutamicum (Tenhaef et al., 2018).

Fig. 1.

Fig. 1

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Schematic overview of the metabolic connection of the Weimberg pathway to the central carbon metabolism of C. glutamicum. Endogenous enzymes of C. glutamicum catalyzing reactions of the Weimberg pathway or spontaneous chemical reactions are highlighted in green, whereas the respective heterologous enzymes originating from C. crescentus are highlighted in red. Abbreviations: XylB, xylose dehydrogenase; XylC, d-1,4-xylono lactonase; XylD, d-xylonate dehydratase; XylX, 2-keto-3-deoxy-d-xylonate dehydratase; XylA, α-ketoglutarate semi aldehyde dehydrogenase; IolG, myo-inositol-2-dehydrogenase; KsaD, α-ketoglutarate semialdehyde dehydrogenase; ODHC, α-ketoglutarate dehydrogenase complex. (For interpretation of the references to colour in this figure legend, the reader is referred to the Web version of this article.)

These studies show that the C. glutamicum wild type, although not capable of d-xylose utilization via the Weimberg pathway or any other catabolic strategy by nature, does already possess individual Weimberg pathway components enabling d-xylose transport and initial d-xylose oxidation. This causes one to wonder whether there are additional endogenous enzymatic activities contributing to d-xylose utilization, which would help to reduce the number of heterologous genes required for establishing the Weimberg pathway in this bacterium.

In this study, we performed an analysis of the C. glutamicum genome in combination with systematic reduction of the xylXABCD operon to identify such enzymes. Furthermore, we exploited the Weimberg pathway for the direct conversion of d-xylose to α-ketoglutarate and could show that this represents a promising strategy for the microbial production of α-ketoglutarate with C. glutamicum.

2. Materials and methods

2.1. Bacterial strains, plasmids, media and growth conditions

All used bacterial strains and plasmids including their characteristics and sources are listed in Table 1. Escherichia coli DH5α, used for cloning purposes only, was routinely cultivated on a rotary shaker (170 rpm, 37 °C) in reaction tubes with 5 mL Lysogeny Broth (LB) medium (Bertani, 1951) or on LB agar plates (LB medium with 1.8 % [wt/vol] agar). All C. glutamicum strains are derived from C. glutamicum ATCC 13032 (Abe et al., 1967) and were aerobically cultivated on a rotary shaker either in reaction tubes (170 rpm, 30 °C) or in baffled shake flasks (130 rpm, 30 °C). As cultivation medium, brain heart infusion (BHI) medium (Difco Laboratories, Detroit, USA) or defined CGXII medium (Keilhauer et al., 1993) supplemented with different d-glucose/d-xylose mixtures were used. For plasmid propagation, kanamycin was added to final concentrations of 25 μg mL−1 (C. glutamicum) or 50 μg mL−1 (E. coli). Where appropriate, the antibiotic spectinomycin was added to a final concentration of 100 μg mL−1. Induction of gene expression was achieved by isopropyl β-d-thiogalactoside (IPTG) supplementation to a final concentration of 1 mM. In general, growth of bacterial strains, cultivated in baffled shake flasks, was followed over time by measuring the optical density at 600 nm (OD600). Cultivations in the microtiter plate format were performed in Flower Plates with optodes using the microbioreactor BioLector (m2plabs, Baesweiler, Germany), enabling online determination of backscatter, pH and dissolved oxygen. BioLector cultivations were routinely inoculated to an OD600 of 1 and incubated at 30 °C, 1300 rpm and 80 % humidity. The total culture volume was always 1 mL and the backscatter gain was set to 15.

Table 1.

Strains and plasmids used in this study.

Strain or plasmid Relevant characteristicsa Source or reference
C. glutamicum strains
ATCC 13032 (WT) biotin auxotroph wild-type strain Abe et al. (1967)
PO6iolT1 Derivative of C. glutamicum ATCC 13032 with two point mutations in the promotor of iolT1, relative to the start codon at position −113 (A→G) and −112 (C→G) respectively (Brüsseler et al., 2018)
PO6iolT1 Δcg0535 Derivative of C. glutamicum PO6iolT1 with in-frame deletion of cg0535 (ksaD) This study
PO6iolT1 ΔodhA Derivative of C. glutamicum PO6iolT1 with in-frame deletion of odhA (cg1280) This study
E. coli strains
DH5α F− Φ80lacZΔM15 Δ(lacZYA-argF)U169 recA1 endA1 hsdR17 (rK–, mK+) phoA supE44 λ– thi-1 gyrA96 relA1 Invitrogen (Karlsruhe, Germany)
BL21 (DE3) F−ompT hsdSB(rB− mB−) gal dcm (DE3) Invitrogen (Karlsruhe, Germany)
C. glutamicum Plasmids
pEKEx3 Specr; C. glutamicum/E. coli shuttle vector for regulated gene expression; (Ptac, lacIQ, pBL1 oriVCg, pUC18 oriVEc) (Gande et al., 2007)
pEKEx3-xylXABCDCc-opt Specr; pEKEx3 derivative for the regulated expression of xylXABCDCc of C. crescentus Radek et al. (2017)
pEKEx3-xylXADCc-opt Specr; pEKEx3 derivative for the regulated expression of xylXADCc of C. crescentus This study
pEKEx3-xylXDCc-opt Specr; pEKEx3 derivative for the regulated expression of xylXDCc of C. crescentus This study
pEKEx3-xylXCc-opt Specr; pEKEx3 derivative for the regulated expression of xylXCc of C. crescentus This study
pEKEx3-xylDCc-opt Specr; pEKEx3 derivative for the regulated expression of xylDCc of C. crescentus This study
pk19mobsacB-Δcg0535 Kanr; plasmid for in-frame deletion of cg0535 (ksaD) This study
pk19mobsacB-ΔodhA Kanr; plasmid for in-frame deletion of odhA (cg1280) This study



E. coli Plasmids
pET-28b(+) Kanr; Vector for overexpression of genes in E. coli, adding an N-terminal hexahistidine affinity tag to the synthesized protein (pBR322 oriVE.c. PT7lacI) Novagen (Darmstadt, vector, Germany)
pET-28b(+)-cg0535 Kanr; pET-28b(+) derivative for the regulated expression of cg0535 (ksaD) of C. glutamicum This study
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a

Kanr; Kanamycin resistance, Specr; Spectinomycin resistance.

2.2. Plasmid and strain construction

All enzymes were purchased from Thermo Scientific (Schwerte, Germany) whereas codon-optimized synthetic genes for expression in C. glutamicum were obtained from Life Technologies (Darmstadt, Germany). Oligonucleotides were synthesized by Eurofins genomics (Ebersfeld, Germany) and are listed in Table 2. For molecular cloning work, standard protocols, e.g. PCR and Gibson were used (Gibson et al., 2009; Sambrook and Russel, 2001). Verification of the constructed plasmids was performed either by restriction analysis or colony PCR. DNA sequencing was conducted at Eurofins Genomics (Ebersberg, Germany). E. coli DH5α was routinely transformed using the RbCl-method, whereas C. glutamicum was always transformed by electroporation followed by an additional heat shock at 46 °C for 6 min (Eggeling and Bott, 2005; Hanahan, 1983). In-frame deletion of odhA and cg0535 (kasD) was performed by two-step homologues recombination using the plasmids pk19mobsacB-ΔodhA and pk19mobsacB-Δcg0535 as previously described (Schäfer et al., 1994).

Table 2.

Oligonucleotides used in this study.

Name DNA Sequence (5′- 3′)
Construction of pEKEx3-xylXADCc-opt
pe3_check fw CGGCGTTTCACTTCTGAGTTCGGC
pe3_check rev GATATGACCATGATTACGCCAAGC
pe3_xylXAD_xylX_fw GCCAAGCTTGCATGCCTGCATAACTAGTATAAGGAGATATAGATATGG
pe3_xylXAD_xylX_rev TTATACTAGCTTATTACAGCAGGCCACG
pe3_xylXAD_xylA_fw GCTGTAATAAGCTAGTATAAGGAGATATAGATATGAC
pe3_xylXAD_xylA_rev TTATACTAGCTTATTAGGACCAGGAGTAGG
pe3_xylXAD_xylD_fw GTCCTAATAAGCTAGTATAAGGAGATATAGATATGC
pe3_xylXAD_xylD_rev CTGTAAAACGACGGCCAGTGTTATTAGTGGTTGTGGCG
Construction of pEKEx3-xylXDCc-opt
pe3_check fw CGGCGTTTCACTTCTGAGTTCGGC
pe3_check rev GATATGACCATGATTACGCCAAGC
pe3_xylXD_xylX_fw GCCAAGCTTGCATGCCTGCAGCTAGTATAAGGAGATATAGATATGGGCGTGTCCGAGTTC
pe3_xylXD_xylX_rev CGGAGCGCATATCTATATCTCCTTATACTAGCTTATTACAGCAG
pe3_xylXD_xylD_fw AGATATAGATATGCGCTCCGCACTGTCC
pe3_xylXD_xylD_rev CTGTAAAACGACGGCCAGTGTTATTAGTGGTTGTGGCGTGGC
Construction of pk19mobsacB- Δcg0535 (ksaD)
rsp CACAGGAAACAGCTATGACCATG
univ CGCCAGGGTTTTCCCAGTCACGAC
cg0535_seq_fw AATCCACTTCTCTTGGTGTCATCGT
cg0535_seq_rev CTTCGAGGACGCGAGTATTCATATT
cg0535_fw_fw TGCATGCCTGCAGGTCGACTATCTACTCCCCAGAGGTTATCG
cg0535_fw_rev CCCATTTATTTGCGGTTGCGGTGATCATG
cg0535_rev_fw CGCAACCGCAAATAAATGGGCTGTACCTC
cg0535_rev_rev TTGTAAAACGACGGCCAGTGCGCTAGATTTAGGCCTTG
Construction of pk19mobsacB-ΔodhA (cg1280)
rsp CACAGGAAACAGCTATGACCATG
univ CGCCAGGGTTTTCCCAGTCACGAC
odhA check fw GAAGCACACTTGTTTAGTGG
odhA check rev CCCGTAGAGATCGGCTGGGT
odhA fw_fw TGCATGCCTGCAGGTCGACTCCATCGCCGCCATCCCTG
odhA fw_rev TAAGCTGCTTCTCAGTACTAGCGCTGCTCACGG
odhA rev_fw CGCTAGTACTGAGAAGCAGCTTATCGAC
odhA rev_rev TTGTAAAACGACGGCCAGTGTCCATTATCGTAGGTGATG
Construction of pET-28b(+)-cg0535
pET16b_fw GATCCCGCGAAATTAATACG
pET16b_rv CAAGACCCGTTTAGAGGCCCC
cg0535_fw CTGGTGCCGCGCGGCAGCCACATGATCACCGCAACCGC
cg0535_rev AAGCTTGTCGACGGAGCTCGTTAACGGTCTATTTCCCGAGG
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2.3. Microbial production of α-ketoglutarate

For initial biomass formation, all constructed C. glutamicum strains were cultivated in 50 mL BHI medium with 10 g/l d-glucose in 500 mL baffled shake flasks at 130 rpm and 30 °C on a rotary shaker. Cells were harvested by centrifugation at 4000 rpm for 10 min, resuspended in defined CGXII medium with either 4 % d-glucose or a 1 % d-glucose/3 % d-xylose mixture and then further cultivated for 40 h at 130 rpm and 30 °C on a rotary shaker. For α-ketoglutarate production, defined CGXII medium with either 4 % d-glucose or a 1 % d-glucose/3 % d-xylose mixture was inoculated to an OD600 of 4. If appropriate, gene expression was induced by adding IPTG to a final concentration of 1 mM.

2.4. Heterologous expression of Cg0535 in E. coli and protein purification

The plasmid pET-28b(+)-cg0535 was transformed into E. coli BL21 for heterologous gene expression of cg0535. Cultivations for this purpose were performed in 10 mL 2xYT medium in baffled shake flasks for 15 h at 37 °C and 130 rpm on a rotary shaker. 1 mL of this culture was used to inoculate an expression culture in 100 mL 2xYT medium with 50 mg L−1 kanamycin and cultivated at 37 °C and 130 rpm. At an optical density of OD600 = 1.5, gene expression was induced by the addition of 0.5 mM IPTG and then further incubated at 18 °C and 130 rpm for 18 h. Cells were harvested by centrifugation for 30 min at 6000 rpm and the cell-free supernatant was discarded. Cell pellets were routinely stored at −80 °C if not further processed the same day. In order to avoid protein degradation, all subsequent steps for protein isolation were performed at 4 °C. Frozen cell pellets were first thawed on an ice-water mixture and resuspended in 15 mL lysis buffer (50 mM Tris-HCl pH 7.6, 100 mM NaCl, 10 mM Imidazole, 5 % Glycerin and 1 mM DTT). Crude cell extracts were obtained by using a Branson Sonifier 250 (intensity, 7; duty cycle, 40 %, 6 min; Branson Ultrasonics, Danbury, USA). After removal of the cellular debris by two centrifugation steps (30 min at 6000 rpm and 45 min at 50,000 rpm) Cg0535 was purified from the protein fraction by affinity chromatography using a GE Äkta pure chromatography system (GE Healthcare Life Sciences, Chicago, USA).

2.5. Kinetic characterization of KsaD (Cg0535)

In all dehydrogenase assays performed, the initial NAD(P)H generation due to KsaD-mediated α-ketoglutarate semialdehyde oxidation was monitored at 340 nm and 30 °C using an Shimadzu UV-1601 Spectrophotometer (Kyoto, Japan). The enzyme assays contained 0–5 mM α-ketoglutarate semialdehyde (FCH Group, Chernigiv, Ukraine, supplied by AKos Consulting & Solutions Deutschland GmbH, Steinen, Germany), 5 mM NAD(P)+, 100 mM Potassium phosphate, pH 7.5. Assays were linear over time and proportional to the protein concentration used.

2.6. Quantification of d-xylose

For quantification of d-xylose, a commercial enzyme assay kit was used according to the manufacturer's instructions (Xylose Assay Kit, Megazymes, Wickow, Ireland). A set of different d-xylose concentrations served as external standards.

2.7. HPLC analysis

Identification and quantification of metabolites was performed using a High Performance Liquid Chromatography (HPLC) 1260 Infinity system (Agilent, Waldbronn, Germany). Separation was achieved by using an Organic acid H+ column (8 %, 300 mm by 7.80 mm; Phenomenex, Torrance, CA, USA) at 80 °C with an isocratic elution program using 5 mM sulfuric acid. For detection of organic acids and d-glucose, a diode array detector (DAD) at 210 nm or a refraction index (RI) detector was used, respectively. Data acquisition and analysis was performed using the Agilent OpenLAB Data Analysis - Build 2.200.0.528 software (Agilent, Waldbronn, Germany).

3. Results

3.1. Identification of an endogenous α-ketoglutarate semialdehyde dehydrogenase activity

Presence of the endogenous dehydrogenase IolG oxidizing d-xylose to 1,4-d-xylonolactone and the observation that hydrolyzation of this lactone can occur spontaneously, indicates that heterologous expression of the xylose dehydrogenase (encoded by xylB) and the d-xylonolactonase (encoded by xylC) from C. crescentus might not be required for establishing the Weimberg pathway in C. glutamicum. Since reduction of the Weimberg pathway encoding operon has not been tried yet, a synthetic operon comprised of codon-optimized genes for 2-keto-3-desoxyxylonate dehydratase (xylX), xylonate dehydratase (xylD) and the α-ketoglutarate semialdehyde dehydrogenase (xylA), all originating from C. crescentus, was constructed. The resulting pEKEx3-xylXADCc-opt plasmid was then transferred to C. glutamicum PO6 iolT1, which is characterized by deregulation of the myo-inositol/proton symporter gene iolT1. Growth of the resulting strain C. glutamicum PO6 iolT1 pEKEx3-xylXADCc-opt was compared to that of C. glutamicum PO6 iolT1 pEKEx3-xylXABCDCc-opt bearing the complete xylXABCD operon from C. crescentus (Fig. 2A). Surprisingly, growth of both strains was indistinguishable (μmax = 0.26 ± 0.006 h−1, μmax = 0.26 ± 0.004 h−1, respectively), indicating that heterologous expression of the xylose dehydrogenase (encoded by xylB) and the xylonolactonase (encoded by xylC) is neither necessary nor beneficial for growth of C. glutamicum.

Fig. 2.

Fig. 2

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Microbioreactor cultivations of C. glutamicum strains engineered for d-xylose utilization via the Weimberg pathway. (A)C. glutamicum PO6iolT1 pEKEx3-xylXABCDCc-opt (black), C. glutamicum PO6iolT1 pEKEx3-xylXADCc-opt (brown) and C. glutamicum PO6iolT1 pEKEx3-xylXDCc-opt (red); (B)C. glutamicum PO6iolT1 pEKEx3-xylXCc-opt (cyan), C. glutamicum PO6iolT1 pEKEx3-xylDCc-opt (green) and C. glutamicum PO6iolT1 pEKEX3 (orange). All strains were cultivated in a BioLector microbioreactor system using defined CGXII medium with 40 g L−1d-xylose as sole carbon and energy source. All data represent mean values from three biological replicates. (For interpretation of the references to colour in this figure legend, the reader is referred to the Web version of this article.)

Motivated by these results, we performed a genome-wide search based on sequence similarity to identify genes potentially encoding for enzymes with XylX-, XylD- or XylA-activity in C. glutamicum ATCC 13032. These analyses suggested that the gene cg0535 could encode for an enzyme having a α-ketoglutarate semialdehyde dehydrogenase activity. However, the predicted protein Cg0535 shares only 25 % sequence identity with XylA of C. crescentus. For a better assessment, secondary structures of Cg0535 and XylA were calculated and aligned using PROMALS3D (PROfile Multiple Alignment with predicted Local Structures and three-dimensional constraints) (Supplementary Fig. S1) (Pei et al., 2008). This in silico analysis revealed a striking resemblance between both proteins with regard to their secondary structure triggering further investigations. To the best of our knowledge, nothing about regulation and expression of cg0535 in C. glutamicum is known. Nonetheless, C. glutamicum PO6 iolT1 pEKEx3-xylXDCc-opt with a further reduced operon was constructed to find out whether heterologous expression of xylA from C. crescentus is required for establishing the Weimberg pathway in C. glutamicum. Comparative cultivation of C. glutamicum PO6 iolT1 pEKEx3-xylXDCc-opt and C. glutamicum PO6 iolT1 pEKEx3-xylXADCc-opt revealed that C. glutamicum indeed does have an endogenous α-ketoglutarate semialdehyde dehydrogenase as both strains exhibited the same growth rate (μmax = 0.26 ± 0.008 h−1, μmax = 0.26 ± 0.006 h−1, respectively) (Fig. 2A). Subsequently, cg0535 was deleted in the genome of C. glutamicum PO6 iolT1, yielding C. glutamicum PO6 iolT1 Δcg0535. After transformation of this strain with pEKEx3-xylXDCc-opt, the resulting strain C. glutamicum PO6 iolT1 Δcg0535 pEKEx3-xylXDCc-opt was compared to its parent strain C. glutamicum PO6 iolT1 pEKEx3-xylXDCc-opt. These experiments showed that deletion of cg0535 completely abolished growth of C. glutamicum PO6 iolT1 Δcg0535 pEKEx3xylXDCc-opt confirming that Cg0535 indeed has α-ketoglutarate semialdehyde dehydrogenase activity (data not shown). The inability of the cg0535 deletion mutant to grow on d-xylose also indicates that Cg0535 appears to be the only endogenous enzyme of C. glutamicum significantly contributing to α-ketoglutarate semialdehyde oxidation, at last under the cultivation conditions tested.

With the aim to characterize Cg0535 in more detail, the cg0535 gene was isolated from the genome of C. glutamicum ATCC 13032 by PCR and cloned into the pET-28b(+)-vector for heterologous expression in E. coli BL21 (DE3). Gene expression in E. coli at 100 mL-scale and subsequent protein purification by affinity chromatography yielded 0.6 mg Cg0535 protein. Subsequently, we performed in vitro dehydrogenase assays using α-ketoglutarate semialdehyde as substrate and NAD or NADP as cofactors to determine selected kinetic parameters of Cg0535. These in vitro experiments confirmed the assumed α-ketoglutarate semialdehyde dehydrogenase activity of this enzyme and furthermore revealed a preference for the cofactor NAD as the calculated specific activity (U mg−1) with NAD was three times higher compared to the activity with NADP (51.8 μmol min−1 mg−1 and 15.8 μmol min−1 mg−1, respectively) (Supplementary Fig. S2). Therefore, depending on the cofactor used, different Michaelis constants (Km) for α-ketoglutarate semialdehyde could be calculated (NAD, 0.87 mM; NADP, 0.21 mM). Considering these findings, we would like to introduce the designation ksaD (α-ketoglutarate semialdehyde dehydrogenase) for cg0535 of C. glutamicum.

3.2. Expression of xylD or xylX enables growth on d-xylose

Analysis of the C. glutamicum genome did not identify any hitherto unknown dehydratases potentially catalyzing the two subsequent dehydration reactions of the Weimberg pathway. Noteworthy, enzyme assays conducted with the dehydratases XylX and XylD of C. cresentus showed that both dehydratases accept d-xylonate as substrate (Dahms and Donald, 1982). Since both dehydratase substrates d-xylonate and 2-keto-3-deoxy-xylonate of the Weimberg pathway, are chemically quite similar, it makes one wonder why two separate enzymes appear to be necessary (Fig. 1). Unfortunately, no experimental data shedding more light on this interesting aspect are available for the enzymes of C. crescentus. However, a conducted comparison of both enzymes as part of this study revealed only a low sequence identity (18 %) and an analysis using PROMALS3D suggested two very different secondary structures (data not shown). Nevertheless, driven by curiosity, the plasmids pEKEx3-xylXCc-opt and pEKEx3-xylDCc-opt were constructed and individually introduced into C. glutamicum PO6 iolT1. The resulting strains C. glutamicum PO6 iolT1 pEKEx3-xylXCc-opt and C. glutamicum PO6 iolT1 pEKEx3-xylDCc-opt were compared with regard to growth to C. glutamicum PO6 iolT1 pEKEx3 (Fig. 2B). As a result, both strains expressing either xylX or xylD could grow on this defined medium with d-xylose as sole carbon and energy source, whereas C. glutamicum PO6 iolT1 could not. The growth rates of C. glutamicum PO6 iolT1 pEKEx3-xylXCc-opt and C. glutamicum PO6 iolT1 pEKEx3-xylDCc-opt were identical (μmax = 0.25 ± 0.006 h−1, μmax = 0.25 ± 0.004 h−1, respectively). Apparently, both dehydratases can complement for each other in C. glutamicum and heterologous expression of either xylX or xylD from C. crescentus is sufficient for enabling d-xylose utilization via the Weimberg pathway in C. glutamicum PO6 iolT1.

3.3. α-ketoglutarate synthesis via the Weimberg pathway

The Weimberg pathway represents a shortcut to the biotechnologically interesting TCA-cycle intermediate α-ketoglutarate without loss of carbon as compared to α-ketoglutarate synthesis starting from d-glucose (Fig. 1) (Jo et al., 2012). Nevertheless, microbial production of this dicarboxylic acid from d-xylose via the Weimberg pathway with C. glutamicum has not been investigated, yet. Within the TCA-cycle of C. glutamicum, the large multienzyme α-ketoglutarate dehydrogenase complex (ODHC) is responsible for the oxidative decarboxylation of α-ketoglutarate (Usuda et al., 1996; Bott, 2007). ODHC is comprised of three subunits: E1o (α-ketoglutarate decarboxylase, OdhA), E2 (dihydrolipoamide acetyl/succinyl-transferase, AceF) and E3 (dihydrolipoamide dehydrogenase, Lpd). It could be shown previously, that deletion of odhA results in the accumulation of α-ketoglutarate (Asakura et al., 2007). With the aim of establishing microbial α-ketoglutarate production from d-xylose via the Weimberg pathway in C. glutamicum, odhA was also deleted in C. glutamicum PO6 iolT1. Initially, the resulting strain C. glutamicum PO6 iolT1 ΔodhA was cultivated in defined CGXII medium supplemented with 40 g L−1 d-glucose as the sole carbon and energy source to find out if this is able to overproduce α-ketoglutarate from this hexose. Within 120 h, this strain accumulated 5.76 ± 0.06 g L−1 (39.43 ± 0.4 mM) α-ketoglutarate in the supernatant (Fig. 3). In contrast, the parent strain C. glutamicum PO6 iolT1 without deletion of odhA accumulated only 0.05 ± 0.00 g L−1 (0.37 ± 0.03 mM) α-ketoglutarate. Subsequently, C. glutamicum PO6 iolT1 ΔodhA was transformed with pEKEx3-xylXABCDCc-opt to find out whether the resulting strain accumulates more α-ketoglutarate in d-glucose/d-xylose mixtures. Noteworthy, deletion of odhA interrupting the TCA-cycle renders cultivation on d-xylose as sole carbon and energy source impossible. Here, C. glutamicum PO6 iolT1 ΔodhA pEKEx3-xylXABCDCc-opt accumulated 7.92 ± 0.13 g L−1 (54.21 ± 0.86 mM) α-ketoglutarate in the supernatant when cultivated in defined CGXII medium with 10 g L−1 d-glucose and 30 g L−1 d-xylose (Fig. 3). In comparison to cultivation of C. glutamicum PO6 iolT1 ΔodhA in defined medium containing only d-glucose, the product titer could be increased 1.5-fold. Motivated by these findings, C. glutamicum PO6 iolT1 ΔodhA pEKEx3-xylXCc-opt and C. glutamicum PO6 iolT1 ΔodhA pEKEx3-xylDCc-opt were also constructed and characterized with regard to their α-ketoglutarate production capabilities on d-glucose/d-xylose mixtures. Interestingly, both strains accumulated much less α-ketoglutarate in the supernatant compared to the strain with the full xylXABCD-operon (1.27 ± 0.1 g L−1 (8.71 ± 0.7 mM) and 1.26 ± 0.0 g L−1 (8.62 ± 0.0 mM, respectively). This was somewhat surprising, as these results hint towards a limitation of the flux through the Weimberg pathway during product formation, which was not observable during growth experiments with C. glutamicum strains without odhA-deletion. Subsequent construction and characterization of C. glutamicum PO6 iolT1 ΔodhA pEKEx3-xylXDCc-opt, bearing the plasmid for expression of both dehydratase genes from C. crescentus, supports the hypothesis of a restricted flux through the Weimberg pathway in this strain background because an increased α-ketoglutarate concentration of 3.30 ± 0.09 g L−1 (22.61 ± 0.65 mM) could be determined in the supernatant.

Fig. 3.

Fig. 3

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Accumulation of α-ketoglutarate during shake flask cultivations of different C. glutamicum strains in defined CGXII medium supplemented with either 40 g L−1d-glucose or a mixture of 10 g L−1d-glucose and 30 g L−1d-xylose. C. glutamicum PO6iolT1 (orange, 40 g L−1d-glucose), C. glutamicum PO6iolT1 ΔodhA (purple, 40 g L−1d-glucose), C. glutamicum PO6iolT1 ΔodhA pEKEx3-xylXABCDCc-opt (black, 10 g L−1d-glucose and 30 g L−1d-xylose), C. glutamicum PO6iolT1 ΔodhA pEKEx3-xylXDCc-opt (red, 10 g L−1d-glucose and 30 g L−1d-xylose), C. glutamicum PO6iolT1 ΔodhA pEKEx3-xylXCc-opt (cyan, 10 g L−1d-glucose and 30 g L−1d-xylose), C. glutamicum PO6iolT1 ΔodhA pEKEx3-xylDCc-opt (green, 10 g L−1d-glucose and 30 g L−1d-xylose). The data represent mean values and standard deviations obtained from three independent cultures. (For interpretation of the references to colour in this figure legend, the reader is referred to the Web version of this article.)

4. Discussion

Functional introduction of a pathway from another organism or implementation of a novel synthetic pathway usually means addition of new enzymatic activities to the catalytic repertoire of the respective host organism. However, sometimes the “new” enzymes have overlapping substrate specificities with endogenous enzymes rendering their introduction unnecessary. This could be already shown for C. glutamicum R and C. glutamicum ATCC 13032 when establishing the two-step Isomerase pathway for d-xylose utilization as both strains already have a xylulokinase (XylB) and thus only require a heterologous gene encoding for a xylose isomerase (Kawaguchi et al., 2006). In case of Pseudomonas sp., it could be demonstrated that the periplasmic glucose dehydrogenase (Gcd) also contributes to d-xylose utilization via the Weimberg pathway (Köhler et al., 2015; Meijnen et al., 2009). Similarly, an enzymatic study not directly connected to growth on d-xylose revealed that the two endogenous myo-inositol dehydrogenases IolG1 and IolG2 of Lactobacillus casei BL23 can convert d-xylose to d-xylonate similar to IolG of C. glutamicum (Aamudalapalli et al., 2018).

The endogenous α-ketoglutarate semialdehyde dehydrogenase (KsaD) of C. glutamicum discovered in the context of this study is characterized by a high specific activity (51.8 μmol min−1 mg−1), which is comparable to that of the enzyme with the same activity in P. putida (53 μmol min−1 mg−1) (Adams and Rosso, 1967). In the genome of C. glutamicum, the open reading frame of ksaD overlaps with that of cg0536 encoding for a putative 5-dehydro-4-deoxyglucarate dehydratase. This finding hints towards a potential role of KsaD in a putative oxidative pathway for the utilization of sugar acids such as d-galacturonic acid or d-glucuronic acid as theses pathways require α-ketoglutarate semialdehyde dehydrogenase- and 5-dehydro-4-deoxyglucarate dehydratase activities (Richard and Hilditch, 2009; Pick et al., 2016). It sounds reasonable that C. glutamicum has such a catabolic pathway as these sugar derivatives typically to be found in pectin-rich fruits and vegetables such as grapes, apples, bean sprouts should be readily available in the natural habitat of this soil bacterium (Li et al., 2016).

Heterologous expression of either xylX or xylD in C. glutamicum PO6 iolT1 enables growth in d-xylose containing media, indicating that both dehydratases from C. crescentus catalyze both dehydration reactions of the Weimberg pathway in C. glutamicum. In contrast, a P. putida S12 strain equipped with the Weimberg pathway from C. crescentus inevitably requires the expression of xylD whereas heterologous expression of xylX alone is not sufficient for enabling growth on d-xylose (Meijnen et al., 2009). In this case, it was assumed that the endogenous dehydratase PP2836 of P. putida S12 exhibiting 57 % sequence identity to XylX from C. crescentus renders heterologous xylX expression unnecessary. However, this is somewhat puzzling as it would mean that the two dehydratases from C. crescentus cannot complement for each other. Unfortunately, the importance of having both dehydratase has not been studied in C. crescentus as the natural source of both enzymes yet. A detailed kinetic characterization of both dehydratases could shed more light on this important aspect. Noteworthy in this context, the archaeon Haloferax volcanii, naturally having the Weimberg pathway, requires the activity of both dehydratases (HVO_B0038A and HVO_B0027) for growth on d-xylose containing media (Johnsen et al., 2009).

In our experiments, microbial synthesis of α-ketoglutarate from a d-glucose/d-xylose mixture with engineered C. glutamicum strains having the Weimberg pathway turned out to be more beneficial for product formation compared to cultivations using d-glucose as only substrate. This could be a direct consequence of the carbon efficiency of the Weimberg pathway offering a theoretical product yield of 100 %. In contrast, α-ketoglutarate synthesis from d-glucose is always accompanied by loss of carbon as CO2 during isocitrate oxidation in the TCA-cycle, which eventually only allows for a maximum theoretical yield of 83 %. However, we could observe that reduction of the xylXABCD-operon also reduced final product concentrations in the constructed odhA-deletion strains. At this stage, we can only speculate that deletion of odhA, necessary for the accumulation of significant amounts of α-ketoglutarate, causes this effect as this is the only genetic difference to the other d-xylose consuming C. glutamicum strains evaluated in the context of xylXABCD-operon reduction. However, this indicates that heterologous expression of the whole pentacistronic xylXABCD-operon might not be necessary for growth of C. glutamicum in d-xylose containing defined medium, but is beneficial for product formation via the Weimberg pathway, especially in more engineered strains.

5. Conclusions

Reduction of the Weimberg pathway encoding operon from C. crescentus revealed that sole expression of xylX (2-keto-3-deoxy-xylonate-dehydratase) or xylD (xylonate dehydratase) is sufficient for establishing this five-step pathway in C. glutamicum. Reason for this is that C. glutamicum is already equipped with two dehydrogenases conferring the capacity to oxidize d-xylose and α-ketoglutarate semialdehyde. A lactonase converting 1,4-d-xylonolactone to d-xylonate is not required as hydrolyzation of this lactone can occur spontaneously. Conducted experiments employing the carbon efficient Weimberg pathway for the microbial synthesis of α-ketoglutarate indicate that d-xylose might represent a more suitable substrate for the production of this organic acid compared to d-glucose.

Acknowledgements

This work was funded by the German Federal Ministry of Education and Research (BMBF, Grant. No. 031L0015) as part of the project “XyloCut − Shortcut to the carbon efficient microbial production of chemical building blocks from lignocellulose-derived d-xylose”, which is embedded in the ERASysAPP framework.

Footnotes

Appendix A

Supplementary data to this article can be found online at https://doi.org/10.1016/j.mec.2019.e00090.

Appendix A. Supplementary data

The following is the supplementary data to this article:

Supplementary
mmc1.pdf (363.4KB, pdf)

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