Open Access

Combinatorial engineering of hybrid mevalonate pathways in Escherichia coli for protoilludene production

Contributed equally
Microbial Cell Factories201615:14

Received: 10 November 2015

Accepted: 4 January 2016

Published: 19 January 2016



Protoilludene is a valuable sesquiterpene and serves as a precursor for several medicinal compounds and antimicrobial chemicals. It can be synthesized by heterologous expression of protoilludene synthase in Escherichia coli with overexpression of mevalonate (MVA) or methylerythritol-phosphate (MEP) pathway, and farnesyl diphosphate (FPP) synthase. Here, we present E. coli as a cell factory for protoilludene production.


Protoilludene was successfully produced in E. coli by overexpression of a hybrid exogenous MVA pathway, endogenous FPP synthase (IspA), and protoilludene synthase (OMP7) of Omphalotus olearius. For improving protoilludene production, the MVA pathway was engineered to increase synthesis of building blocks isopentenyl diphosphate (IPP) and dimethylallyl diphosphate (DMAPP) by sequential order permutation of the lower MVA portion (MvL), the alteration of promoters and copy numbers for the upper MVA portion (MvU), and the coordination of both portions, resulting in an efficient entire MVA pathway. To reduce the accumulation of mevalonate observed in the culture broth due to lower efficiency of the MvL than the MvU, the MvL was further engineered by homolog substitution with the corresponding genes from Staphylococcus aureus. Finally, the highest protoilludene production of 1199 mg/L was obtained from recombinant E. coli harboring the optimized hybrid MVA pathway in a test tube culture.


This is the first report of microbial synthesis of protoilludene by using an engineered E. coli strain. The protoilludene production was increased by approx. Thousandfold from an initial titer of 1.14 mg/L. The strategies of both the sequential order permutation and homolog substitution could provide a new perspective of engineering MVA pathway, and be applied to optimization of other metabolic pathways.


Protoilludene Escherichia coli Mevalonate pathway Sequential order permutation Homolog substitution


Protoilludene derivatives, including illudins, marasmanes and melleolides, are known to exert antitumor and antimicrobial activities [13]. For example, the most brilliant potential anticancer agent illudin S, which is first isolated from Omphalotus olearius mushroom, has been studied extensively owing to its cytotoxicity to various tumor cell types [4]. These biological properties and medicinal potential have attracted considerable attention since the late 1960s. Illudins, marasmanes and melleolides can be synthesized from protoilludene by different oxygenation reactions. For example, P450 monooxygenases for the biosynthesis of illudin have been identified from O. olearius [5]. However, protoilludene is naturally produced in a small quantity and its purification from biological material suffers from low yields. Hence, metabolic engineering of microorganisms, such as Escherichia coli, is an alternative and attractive route for the production of protoilludene.

Protoilludene biosynthesis begins with the formation of the universal precursors, isopentenyl pyrophosphate (IPP) and dimethylallyl pyrophosphate (DMAPP), which can be generated via the methylerythritol-phosphate (MEP) pathway and the mevalonate (MVA) pathway [6]. Isopentenyl pyrophosphate and dimethylallyl pyrophosphate are condensed to form farnesyl diphosphate (FPP) by FPP synthase. Linear FPP undergoes multiple electrophilic cyclizations and rearrangements to generate tricyclic protoilludene with an action of protoilludene synthase, which has been isolated from various species including O. olearius, Armillaria gallica, and Stereum hirsutum [79]. O. olearius protoilludene synthase (OMP7) exhibits a superior catalytic efficiency (Kcat/Km) of (13.0 ± 2.0) × 104 M−1 s−1 among those protoilludene synthases (Additional file 1: Table S1) [8].

The entire protoilludene synthesis pathway via the MVA pathway can be divided into three portions, referred to as “MvU” composed of acetyl-CoA acetyltransferase/3-hydroxy-3-methylglutaryl-CoA reductase (MvaE) and 3-hydroxy-3-methylglutaryl-CoA synthase (MvaS), “MvL” composed of mevalonate kinase (MvaK1), phosphomevalonate kinase (MvaK2), diphosphomevalonate decarboxylase (MvaD) and IPP isomerase (IDI), and “AO” composed of FPP synthase (IspA) and protoilludene synthase (OMP7) (Fig. 1). The MVA pathway has been widely engineered for production of several sesquiterpenes in E. coli [6, 1012]. In this study, MVA pathway was engineered for a balanced expression of MvU and MvL portions to increase protoilludene production. The MvL portion was optimized by sequential permutation of its constituent genes in consideration of transcriptional polarity, a general tendency of lower expression of the genes distant from promoter in a multi-cistronic operon [13]. In the optimized MvL portion by the random sequential permutation, the constituent genes would be arranged in their activities from low to high activities in the operon. The expression of MvU portion was modulated by changes of promoters and copy-numbers to tune mevalonate production to its utilization by MvL portion. Optimal coordination of the MvUs and MvLs portions of the MVA pathway were finally able to increase protoilludene production from 1.14 to 721 mg/L. As accumulation of mevalonate intermediate was observed in the culture broth, MvL portion was further engineered by substituting its constituent genes with their homologues from Staphylococcus aureus. By the homolog substitution, protoilludene production was increased from 721 to 1199 mg/L in a test tube culture. The successful production of protoilludene from E. coli is shown in this work and the recombinant E. coli harboring the combinatorially engineered hybrid MVA pathway can serve as a basic platform host for production of other valuable terpenoids.
Fig. 1

Schematic diagram of protoilludene biosynthesis via mevalonate (MVA) pathway. Protoilludene biosynthesis pathway is divided into three portions: MvU (acetyl-CoA to mevalonate), MvL (mevalonate to IPP and DMAPP) and AO (IPP and DMAPP to protoilludene). MvU portion is composed of MvaE (HMG-CoA reductase/acetyl-CoA acetyltransferase) and MvaS (HMG-CoA synthase). MvL portion is comprised of MvaK1 (mevalonate kinase), MvaK2 (phosphomevalonate kinase), MvaD (diphosphomevalonate decarboxylase) and IDI (IPP isomerase). AO portion consists of IspA (FPP synthase) and OMP7 (protoilludene synthase). Illudins, marasmanes and melleolides are protoilludene derivatives. Pathway intermediates for protoilludene synthesis are as follows: A-CoA, acetyl-CoA; AA-CoA, acetoacetyl-CoA; HMG-CoA, hydroxymethylglutaryl-CoA; MVAP, phosphomevalonate; MVAPP, diphosphomevalonate; IPP, isopentenyl diphosphate; DMAPP, dimethylallyl diphosphate; and FPP, farnesyl diphosphate. Solid and dashed arrows indicate the identified and unidentified reactions, respectively

Table 1

Strains used in this study




E. coli AO

E. coli DH5α harboring pTAO

This study

E. coli AO/NA

E. coli DH5α harboring pTAO and pSNA

This study

E. coli AO/MvL1–6

E. coli DH5α harboring pTAO and pSMvL1–6

This study

E. coli AO/L1–L6

E. coli DH5α harboring pTAO, pSMvL1–6 and pBMvUL

This study

E. coli AO/M1–M13

E. coli DH5α harboring pTAO and pSMvL1–13-MvUM

This study

E. coli AO/H1–H13

E. coli DH5α harboring pTAOMvUH and pSMvL1–13

This study

This table is a brief description of strains used in this study. For more detailed information, refer to Additional file 1: Table S4

Results and discussion

Establishment of a protoilludene biosynthesis pathway in E. coli

Up to now, 6 protoilludene synthases from three species were identified (Additional file 1: Table S1) [79]. Among them, O. olearius protoilludene synthase (OMP7) exhibits the highest catalytic efficiency which is higher than its homologs OMP6 and Stehi1|73029 by 10 and 30 times, respectively. In order to synthesize protoilludene in E. coli, a codon-optimized OMP7 gene was assembled with E. coli FPP synthase gene (ispA) to construct plasmid pTAO (Fig. 2a). It was transformed into E. coli DH5α, resulting in the strain E. coli AO. This strain was then cultivated at 30 °C for 48 h in 2YT medium containing 2 % (v/v) of glycerol with overlaying 1 mL decane. Gas chromatographic (GC) analysis showed a new peak which was identified as protoilludene by gas chromatograph–mass spectrometer (GC–MS), and corresponded to 1.14 mg/L of protoilludene. The tiny production could be ascribed to an insufficient supply of IPP and DMAPP from the native MEP pathway.
Fig. 2

Establishment of a protoilludene biosynthesis pathway in E. coli a Expression construct of AO portion. AO operon, which is composed of FPP synthase ispA from E. coli and protoilludene synthase OMP7 from O. olearius, is cloned into pTrc99A vector and designated as pTAO. Ec, the gene from E. coli; Oo, the gene from O. olearius. b Identification of protoilludene product. The decane phase from two-phase culture of E. coli AO/NA strain was subjected to GC and GC–MS analysis. c Protoilludene production and mevalonate accumulation in culture of the strain E. coli AO/NA. The strain was grown at 30 °C in 4 mL of 2YT medium with 2 % (v/v) glycerol for 24 and 48 h, and overlaid with 1 mL of decane. The dark gray and light gray bars indicate protoilludene production and mevalonate accumulation, respectively

Thus, the protoilludene synthesis plasmid pTAO was co-transformed with plasmid pSNA [14], which encodes a hybrid exogenous MVA pathway for sufficient supply of IPP and DMAPP, into E. coli DH5α, resulting in the strain E. coli AO/NA. Gas chromatographic analysis showed a specific peak with retention time of 5.7 min, which was subsequently confirmed as protoilludene by GC–MS (Fig. 2b). For 48 h of culture, the strain E. coli AO/NA produced 517 mg/L of protoilludene with an undesired accumulation of mevalonate as much as 571 mg/L (Fig. 2c), indicating the suboptimal performance of MVA pathway encoded by pSNA. It is thus required to redesign the MVA pathway, especially the lower portion of the MVA pathway for protoilludene production.

Optimization of the MvL portion of the MVA pathway by sequential order permutation

Expression levels of genes in an operon are known to be affected by their position within the operon [13]. If a gene is located at the tail end of the operon, its expression level is generally lower. Thus, relative expression levels of multi-genes in an operon can be affected by the sequential order of genes in the operon. A specific metabolic pathway encoded by an operon can be optimized by positional modulation of the constituent genes in the operon. Such an approach has been successfully applied to optimization of zeaxanthin synthetic pathway in Bacillus subtilis [15]. The MvL portion of pSNA is composed of four genes SnMvaK1, SnMvaK2 and SnMvaD from Streptococcus pneumoniae, and IDI from E. coli [10]. Optimization of the MvL portion was performed by sequential order permutation of three genes SnMvaK1, SnMvaK2 and SnMvaD. The four genes were assembled in a “Biobrick” [16] fashion to construct six sequential order permutated lower MVA pathway plasmids (pSMvL1–6) based on pSTV28 vector (Fig. 3a). The strains E. coli AO/MvL1–6 resulting from the co-transformation of pSMvL1–6 and pTAO were evaluated for protoilludene production with supplementation of 4 mM (592.6 mg/L) (R, S)-mevalonate (Fig. 3b). The protoilludene production varied with the sequential order permutation in the MvLs. The highest protoilludene production of 137 mg/L was obtained from E. coli AO/MvL2, whereas E. coli AO/MvL4–6 produced low titers of protoilludene below 25 mg/L. Around 80 mg/L of protoilludene was produced from E. coli AO/MvL1, 3. Residual amounts of mevalonate in the culture broth were measured at the end of the culture to observe the consumption by the strains harboring these sequential order permutated plasmids (Additional file 1: Fig. S2). As expected, the mevalonate consumption generally corresponded to the protoilludene production. The residual mevalonate concentrations in culture of E. coli AO/MvL4–6 were as high as 3 mM (438.5 mg/L), whereas the concentrations in E. coli AO/MvL1, 3 and AO/MvL2 were as low as around 1.7 mM (248.5 mg/L) and 1.3 mM (190.0 mg/L), respectively. Therefore, the lower MVA pathway plasmid pSMvL2 is found to have an optimized gene order for the best performance of the MvL portion, and its order of SnMvaK1-SnMvaD-SnMvaK2-IDI is interestingly consistent with arrangement of the native genes in S. pneumoniae (GenBank: AE007317.1).
Fig. 3

Optimization of the lower (MvL) portion of MVA pathway by sequential order permutation. a Expression constructs of the sequential order permutated MvL portions. MvL operon, containing MvaK1, MvaK2 and MvaD from S. pneumoniae, and IDI from E. coli, is cloned into pSTV28 vector. Sn, the gene from S. pneumoniae; Ec, the gene from E. coli; Plac, lac promoter. b Effect of sequential order permutated MvLs on protoilludene production and cell growth. The strains were grown for 48 h at 30 °C in 4 mL of 2YT medium containing 2 % (v/v) glycerol and 4 mM mevalonate with overlay of 1 mL decane. The dark and light gray bars indicate protoilludene production and cell growth, respectively

Coordination of MvU and MvL portions of MVA pathway for protoilludene production

To optimize the synthesis of mevalonate, the MvU portion of the MVA pathway was cloned into three plasmids with different copy numbers and promoters, pBBR1MCS-2 (6–8 copies and lac promoter), pSTV28 (10–15 copies and lac promoter), and pTrc99A (20–30 copies and trc promoter) [12], which were designated as pBMvUL (LOW), pSMvUM (MEDIUM) and pTMvUH (HIGH), respectively (Fig. 4a). The alternations of copy number and promoter led to the differentiation of mevalonate producing capacity in a range of 104–215 mg/L per OD600 at 48 h (Fig. 4b), although there was no significant difference in cell growth among these three strains (Additional file 1: Fig. S3).
Fig. 4

Coordination of the lower (MvL) and upper (MvU) portions of MVA pathway for protoilludene production. a Expression constructs of the MvU portions with alternations of promoter and copy-number. MvU operon consists of MvaE and MvaS from E. faecalis. The two genes are cloned into pBBR1MCS-2, pSTV28 and pTrc99A vectors, which are designated as pBMvUL, pSMvUM and pTMvUH, respectively. Ef, the gene from E. faecalis; Plac and Ptrc, lac promoter and trc promoter, respectively. Rectangles show replication origin of each plasmid. b Mevalonate production capacity of recombinant E. coli harboring each of pBMvUL, pSMvUM and pTMvUH. The strains were cultured in 2YT medium at 30 °C for 48 h. c and d Effect of combinations of MvUL,M,H and MvL1–6 on protoilludene production and mevalonate accumulation. The culture were carried out in 4 mL of 2YT medium containing 2 % (v/v) glycerol with overlay of 1 mL decane at 30 °C for 48 h

Both MvUs and MvLs were then expressed in all combinations in E. coli to find an optimal combination of the two portions for protoilludene production. As the MvUL plasmid (pBMvUL) is compatible with the lower MVA portion plasmids (pSMvL1–6) and the protoilludene plasmid (pTAO), E. coli can be transformed with the three plasmids for the combination of MvUs and MvLs in protoilludene production. However, the MvUM plasmid (pSMvUM) is not compatible with pSMvL1–6 derived from the same cloning vector (pSTV28) and MvUM and MvL1–6 are combined in pSMvL1–6-MvUM (Additional file 1: Fig. S4). The MvUH portion was cloned into pTAO plasmid, resulting in pTAO-MvUH, because the MvUH plasmid (pTMvUH) is not compatible with the same vector originated pTAO plasmid (Additional file 1: Fig. S4). Escherichia coli AO/H1–H6 strains harboring pTAO-MvUH and pSMvL1–6 produced a little amount of protoilludene (<35 mg/L; Fig. 4c), accompanying with accumulation of a large amount of mevalonate (>1300 mg/L). It indicated the MvUH produced too much mevalonate beyond the capacity of MvLs and the metabolic unbalance between MvUH and MvLs caused even a significant decrease of cell growth (Additional file 1: Table S2). In contrast, there was no significant accumulation of mevalonate in the strains of E. coli AO/L1-L6 (pTAO/pSMvL1–6/pBMvUL) and E. coli AO/M1–M6 (pTAO/pSMvL1-6-MvUM), which suggested the lower capacity of the upper portions MvUL and MvUM than the lower portion MvLs (Fig. 4d). In contrast, strains E. coli AO/L1–L6 and E. coli AO/M1–M6 did not exhibit significant mevalonate accumulation (Fig. 4d). However, the poor mevalonate supply from MvUL compared to MvUM seems to restrict the protoilludene production. The highest protoilludene production of 721 mg/L was observed in E. coli AO/M2, which represented a 1.4-fold increase to the production from E. coli AO/NA.

Homolog substitution of the lower MVA portion genes

Kinetic properties of homolog enzymes from different organisms are generally distinct from each other. Homolog enzymes of the lower MVA portion have also different kinetic properties. For example, S. pneumoniae mevalonate kinase (SnMvaK1) is subject to allosteric regulation by diphosphomevalonate, whereas S. aureus mevalonate kinase (SaMvaK1) without the allosteric regulation is competitively inhibited by isoprenyl diphosphates (DMAPP, IPP and FPP) [17, 18]. A metabolic pathway of interest can be improved by substituting a problematic constituent enzyme with its homolog with a desirable property [14]. In order to further improve the mevalonate pathway, the genes of the lower MVA portion MvL2 in pSMvL2 were substituted with their homologs from S. aureus, resulting into a new set of pSMvL7–13 plasmids (Fig. 5a). The effect of the lower MVA portions MvL7–13 on protoilludene production was investigated in combination with the upper MVA pathway portions MvUM and MvUH in the same manner used in Fig. 4c. The upper MVA portion MvUL was excluded in this study because it was suspected to produce insufficient amount of mevalonate for high production of protoilludene. The plasmids pSMvL7–13-MvUM were constructed to combine the upper portion MvUM and the lower portions MvL7–13(Additional file 1: Fig. S4). The combinations of MvUH and MvL7–13 were conducted by co-transformation of pTAO-MvUH and pSMvL7-13. Interestingly, the strains E. coli AO/M7 (pTAO/pSMvL7-MvUM) and E. coli AO/H7 (pTAO-MvUH and pSMvL7), containing the lower MVA portion MvL7 with homolog substitution of SaMvaK1 only, produced the enhanced protoilludene production of 1199 and 740 mg/L, respectively (Fig. 5b and Additional file 1: Table S3). Other homolog substitutions failed to improve production of protoilludene (Fig. 5b). As the homolog substitution of SaMvaK1 with no allosteric inhibition by diphosphomevalonate is effective for protoilludene production, it is suspected the accumulation of diphosphomevalonate in the strain E. coli AO/M2 harboring the lower MVA portion MvL2 due to some bottleneck in the conversion of diphosphomevalonate to IPP by diphosphomevalonate decarboxylase.
Fig. 5

Optimization of MVA pathway by homolog substitution for the lower portion genes. a Expression constructs of the homolog substituted MvL portions. The homolog genes are from S. aureus and represented with prefixion of “Sa” to the gene name. b and c Effect of combinations of MvUM,H and MvL7–13 on protoilludene production and mevalonate accumulation. The culture were carried out in 4 mL of 2YT medium containing 2 % (v/v) glycerol with overlay of 1 mL decane at 30 °C for 48 h


It is demonstrated the feasibility of producing protoilludene in engineered E. coli. Heterologous expression of the MVA pathway encoded by pSNA enabled the strain E. coli AO/NA to produce 517 mg/L of protoilludene, but mevalonate was accumulated in a significant amount as 571 mg/L due to the unbalanced upper and lower portions of the MVA pathway. To create a balanced efficient MVA pathway, we sequentially permuted the order of genes in the lower portion of the MVA pathway (MvL) and coordinated their expression with the upper portion of the MVA pathway (MvU) by alternations of copy-number and promoter of plasmids. Through this approach, 721 mg/L of protoilludene was produced with reduced accumulation of mevalonate in the strain E. coli AO/M2. The substitution of mevalonate kinase from S. pneumoniae with the homolog from S. aureus further increased protoilludene production to 1199 mg/L. These results suggest that the optimized MVA pathway is efficient to supply IPP and DMAPP for protoilludene production and also can serve as a platform IPP/DMAPP synthesis pathway for production of other valuable terpenes.


Bacterial strains and growth conditions

Escherichia coli DH5α were grown in 2YT medium (16 g tryptone, 10 g yeast extract, and 5 g sodium chloride per 1L) at 37 °C for plasmid construction, and at 30 °C for protoilludene production. The seed culture grown overnight at 37 °C was inoculated with an optical density at 600 nm (OD600) of 0.1 into 2YT medium containing 2 % (v/v) glycerol. Escherichia coli strains  (Table 1) harboring the lower portion of the MVA pathway were cultured with addition of 4 mM mevalonate. Ampicillin (100 μg/mL), chloramphenicol (50 μg/mL), kanamycin (50 μg/mL) and 0.2 mM IPTG were added as required. To harvest protoilludene produced during culture, 1 mL of decane was initially overlaid on 4 mL of culture broth. Cell growth was determined by measuring the OD600. All experiments were carried out in duplicate.

Construction of plasmids

Basic molecular biology procedures, including restriction enzyme digestion and bacterial transformation, were carried out as described in the literature [19]. DNA fragments were amplified by PCR using Pfu DNA polymerase (SolGent, Daejeon, Korea) according to the manufacturer’s instructions. BglBricks assembly [16] was applied for construction of various plasmids. The schematic diagram of the constructs is shown in figures and the detailed construction process was depicted in Additional file 1. All plasmids and primers used in this study are described in Additional file 1: Table S4.

Identification and quantification of protoilludene

The decane phase of the two-phase culture was collected and centrifuged for 10 min at 12,000 rpm to remove cell debris, and subsequently subjected to gas chromatography (GC) and gas chromatography-mass spectrometry (GC–MS). The production of protoilludene was quantified using an Agilent Technologies 7890A gas chromatograph equipped with a flame ionization detector (FID). One μL of sample was injected at a split ratio of 1:10, and separated on a 19091 N-133 HP-INNOWAX column (length, 30 m; internal diameter, 0.25 mm; film thickness, 250 μm). The oven temperature was initially held at 80 °C for 1 min and was increased at a rate of 10 °C/min to 250 °C, where it was held for 1 min. Nitrogen was used as the carrier gas with an inlet pressure of 39 psi. The detector temperature was maintained at 260 °C. GC–MS analysis was run on a GCMS-2010 ultra mass spectrometer (Shimadzu, Tokyo, Japan). Purified protoilludene was used as the standard compound to construct the standard curve (R2 > 0.99) for the estimation of protoilludene production (Additional file 1: Fig. S1).

Quantification of mevalonate

Mevalonate concentration was determined by GC analysis. Culture filtrate was adjusted to pH 2 with 3 M HCl, incubated at 45 °C for 1 h, saturated with anhydrous Na2SO4, and extracted with ethyl acetate. The resulting samples were analyzed for mevalonate concentration using an Agilent Technologies 7890A gas chromatograph. The analytical temperature of the GC was controlled at an initial temperature of 180 °C for 1 min, then ramped to 200 °C gradually at 2.5 °C/min and held for 2 min. The detector temperature was maintained at 260 °C.



Authors’ contributions

SWK and CW conceived the idea and designed the experiments. LY carried out the experiments. LY, CW and JZ analyzed the data. LY, SWK and CW drafted the manuscript. All authors read and approved the final manuscript.


This work was supported by a Grant (NRF-2013R1A1A2008289) and a Grant (NRF-2012M1A2A2671831) from the National Research Foundation, MSIP and a Grant from the Next-Generation BioGreen 21 Program (SSAC, Grant#: PJ01106201), Rural Development Administration, Korea.

Competing interests

The authors declare that they have no competing interests.

Open AccessThis article is distributed under the terms of the Creative Commons Attribution 4.0 International License (, which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made. The Creative Commons Public Domain Dedication waiver ( applies to the data made available in this article, unless otherwise stated.

Authors’ Affiliations

Division of Applied Life Science (BK21 Plus Program), PMBBRC, Gyeongsang National University
Faculty of Life Science and Food Engineering, Huaiyin Institute of Technology


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