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Applied and Environmental Microbiology, December 2008, p. 7802-7808, Vol. 74, No. 24
0099-2240/08/$08.00+0 doi:10.1128/AEM.02046-08
Copyright © 2008, American Society for Microbiology. All Rights Reserved.

Department of Chemical and Biomolecular Engineering, University of California, Los Angeles, 5531 Boelter Hall, 420 Westwood Plaza, Los Angeles, California 90095
Received 3 September 2008/ Accepted 20 October 2008
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Because of the growth requirement for amino acids, keto acid biosynthesis is amenable to directed evolution using growth-based selection. Here, we evolved a synthetic pathway for the production of 1-propanol and 1-butanol in E. coli by using a 2-keto acid-based selection strategy. No microorganisms have been identified to produce 1-propanol from glucose in industrially relevant quantities, although small amounts have been identified as microbial by-products. 1-Propanol can be esterified to yield diesel fuels and be dehydrated to yield propylene, which is currently derived from petroleum as a monomer for making polypropylene. 1-Butanol has been proposed as a supplement of gasoline as a transportation fuel. It is traditionally produced using Clostridium species, and its production using E. coli has just begun to be explored (1, 13). 1-Propanol and 1-butanol can be synthesized through 2-ketobutyrate (2) via the KDC and ADH pathway (Fig. 1).
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FIG. 1. Schematic representation of the pathway for 1-propanol and 1-butanol production. The engineered citramalate pathway consists of four enzymatic steps from pyruvate to 2-ketobutyrate.
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However, heterologous proteins are not always active in foreign hosts and thermophilic enzymes often lose activities at moderate temperatures. To improve the activity of CimA, we employed a directed evolution strategy (10). Because 2-keto acids are precursors of amino acids, these metabolites are essential and can be used as a selection in directed evolution. Here, we have achieved increased production of 1-propanol and 1-butanol by applying a selection based on the requirement of L-isoleucine.
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Strains and plasmids.
A list of many of the strains and plasmids used is in this study is given in Table 1.
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TABLE 1. Strains used in this study
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To remove the noncoding region in pSA121, pSA121 was used as PCR template with primers A113 and A227 (5'-ACGCAGTCGACCTACAATTTTCCAGTAACTTCTCTA-3'). PCR products were digested with Acc65I and SalI and cloned into pSA63 cut with the same enzymes, creating pSA125.
For protein overexpression and purification, cimA and cimA3.7 were amplified with primers A261 (5'-CGGGATCCGGTAAGGATATTTGATACAACACTTA-3') and A114 and A261 and A227, respectively. PCR products were digested with BamHI and SalI and cloned into pETDuet-1 (Novagen (Madison, WI) cut with the same enzymes, creating pSA153 and pSA154.
Medium and culture conditions for 1-propanol and 1-butanol production.
M9 medium containing 72 g/liter glucose, 5 g/liter yeast extract, 100 µg/ml ampicillin, 30 µg/ml kanamycin, and a 1:1,000 dilution of Trace metal mix A5 [2.86 g H3BO3, 1.81 g MnCl2·4H2O, 0.222 g ZnSO4·7H2O, 0.39 g Na2MoO4·2H2O, 0.079 g CuSO4·5H2O, 49.4 mg Co(NO3)2·6H2O per liter of water] was used for cell growth. Preculture in test tubes containing 3 ml of medium was performed at 37°C overnight on a rotary shaker (250 rpm). Overnight culture was diluted 1:100 into 20 ml of fresh medium in a 250-ml screw cap conical flask. Cells were grown at 37°C for 3 h, followed by addition of 0.1 mM isopropyl-β-D-thiogalactopyranoside (IPTG). Cultivation was performed at 30°C on a rotary shaker (250 rpm). Gas chromatography-flame ionization detection and high-performance liquid chromatography analyses were carried out as previously described (2).
Directed evolution.
Error-prone PCR was carried out as described previously (3) using pSA63 (Table 1) as a template. A plasmid library of cimA variants was constructed on pSA63 by ligating the error-prone PCR product digested with Acc65I and SalI. Ten microliters of the ligation reaction was used to transform 100 µl of XL10 Gold cells (Stratagene, La Jolla, CA). The resultant library size was calculated (
1 x 106 colonies), and the plasmid library was amplified on LB agar plates containing 30 µg/ml kanamycin. SA405 or SA408 was transformed with the plasmid library. The cells were incubated in 20 ml of M9 medium containing 10 g/liter glucose and 30 µg/ml kanamycin with shaking at 30°C for 3 days. Plasmids were purified from the resulting cultures. DNA shuffling was carried out as described previously (21), except that KOD DNA polymerase was used for fragment amplification. A plasmid library construction and liquid culture selection were carried out as described above. The resulting cultures were spread out on M9 agar plates containing 10 g/liter glucose and 30 µg/ml kanamycin. The plates were incubated at 30°C for 3 days.
Protein purification.
The wild-type CimA and CimA3.7 were synthesized from pSA153 and pSA154 in E. coli strain BL21 Star (DE3) (Invitrogen, Carlsbad, CA), followed by purification with Ni-nitrilotriacetic acid spin columns (Qiagen, Valencia, CA). Protein concentrations were determined by the Bradford assay (Bio-Rad, Hercules, CA).
Citramalate synthase assay.
The CimA enzyme activity was assayed by monitoring the production of CoA over time (8, 14). Purified proteins (0.1 µM) were dissolved in 150 µl of TES buffer (0.1 M [pH 7.5]) containing various concentrations of acetyl-CoA and pyruvate. The production of CoA was confirmed to be linear over 1 h. After incubation at various temperatures for 1 h, 50 µl of 10 mM5,5'-dithio-bis(2-nitrobenzoic acid) in 0.1 M Tris-HCl (pH 8.0) was added to measure the appearance of the free SH group of the released CoA SH. The absorbance at 412 nm was recorded. The concentrations of CoASH produced were calculated from a standard curve generated with various concentrations of 2-mercaptoethanol.
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ilvA and
tdcB) transformed with pSA63 (harboring wild-type cimA) (Fig. 2A), pCS27 (without cimA and leuABCD), or the wild-type strain (JCL16) (Fig. 2B). SA405 cells not expressing CimA were unable to grow without L-isoleucine (Fig. 2B). The citramalate pathway rescued the growth of SA405 under the same condition, although the growth rate of SA405 with the citramalate pathway was lower than that of JCL16 or SA405 with L-isoleucine (Fig. 2B).
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FIG. 2. Transfer of the citramalate pathway to E. coli. (A) Schematic representation of the synthetic operons. (B) Time courses for the growth of E. coli strain SA405 ( ilvA tdcB) and JCL16. OD600, optical density at 600 nm. Cells were incubated in M9 medium containing glucose at 30°C. Diamonds, JCL16; circles, squares, and triangles, SA405 with pSA63 (circles), pCS27 (without cimA-leuABCD) (squares), or L-isoleucine (39.5 µg/ml) (triangles).
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FIG. 3. Progress of the evolution of CimA. (A) Amino acid mutations are shown in the schematic representation of CimA. The gray bar indicates the putative regulator domain. (B) Time courses for the growth of an E. coli strain (SA408 [ ilvA tdcB ilvI]) containing the derivative of pSA63 (cimA-leuABCD). Cells were incubated in M9 medium containing glucose at 30°C. Circles, wild-type (WT) CimA; triangles, CimA2; diamonds, CimA3.7; and squares, control (blank plasmid).
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ilvA and
tdcB in the host (designated as SA408). IlvI is the large subunit of acetohydroxy acid synthase III (AHAS III), which exhibits a higher specificity toward 2-ketobutyrate (6).The remaining isozyme (AHAS I), encoded by the ilvBN genes, has higher specificity to pyruvate than to 2-ketobutyrate (6). Since the endogenous concentrations of 2-ketobutyrate (
10 µM) are much lower than Km value for 2-ketobutyrate of AHAS I (
5 mM) (5), the deletion of ilvI decreases the flux from 2-ketobutyrate to isoleucine and thus requires more 2-ketobutyrate to synthesize isoleucine through the less efficient isozyme. After the fourth round, eight colonies were randomly picked. We sequenced the cimA variant that produced the largest amount of alcohols (denoted cimA2 [Fig. 3A]). In addition to the amino acid substitutions in CimA1, CimA2 contains two new amino acid substitutions (His126Gln and Thr204Ala) and a frameshift mutation at bp 1117, creating a CimA variant missing the C-terminal domain from the 373rd residue.
The cimA2 mutant contains a stop codon at bp 1117, indicating that this operon contains
350 bp of noncoding region between the cimA gene and the leuA gene located on the synthetic operon. It has been known that large noncoding regions decrease mRNA stability and translational efficiency (11). To eliminate the possibility of an expression deficiency of leuABCD downstream of cimA, we removed the noncoding region from the plasmid (denoted CimA2
[Fig. 3A]). CimA2
was subjected to the next two generations of mutagenesis, selection, and screening using the same scheme as the last two rounds.
After the sixth round, nine colonies were randomly picked for sequencing (Fig. 3A). The selected cimA mutants were recloned into pSA63 to remove the possibility of extra mutations in the plasmid. We did not observe any apparent hot spots of mutations (Fig. 3A), and all mutations were outside of the active site (Fig. 3A).
Growth rates were compared for SA408 (
ilvA
tdcB
ilvI) transformed with pSA63 (harboring wild-type cimA) (Fig. 2A), pSA121 (containing cimA2), pSA142 (containing cimA3.7), or pCS27 (without cimA and leuABCD) (Fig. 3B). The growth rate of strains expressing CimA2 or CimA3.7 was higher than that of the strain expressing wild-type CimA. Cells not expressing CimA were unable to grow under the same conditions (Fig. 3B). The strains with the other CimA3 variants showed growth similar to that of the strain with CimA3.7 (data not shown). These results indicate that growth depends on the activity of CimA to supply precursors for L-isoleucine production.
Purification and characterization of wild-type and evolved CimA.
The wild-type CimA and CimA3.7 were expressed from a His tag plasmid (pSA153 or pSA154) and purified as described in Materials and Methods. The kinetic parameters were measured for both of these proteins by monitoring the production of CoA in the presence of pyruvate and acetyl-CoA at 30°C. The kcat and Km for pyruvate and for acetyl-CoA of the wild type and CimA3.7 were determined (Table 2). The kcat and Km for acetyl-CoA of CimA3.7 improved about threefold over the wild-type levels. However, the Km for pyruvate of CimA3.7 increased over wild-type CimA, although this may not be crucial for the activity in vivo as the cellular concentration of pyruvate (7.5 mM) (20) is much higher than the Km for pyruvate (0.34 mM) of CimA3.7.
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TABLE 2. Kinetic parameters of the wild-type CimA and CimA3.7
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FIG. 4. Enzyme assays. (A) Specific activities (M CoA produced/min/M protein) of the wild type (WT) (squares) and CimA3.7 (circles) at various temperatures. (B) Specific activities of the wild type and CimA3.7 at 30°C in the presence of various concentrations of L-isoleucine.
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1-Propanol and 1-butanol production with CimA.
The next task was to use the citramalate pathway to enhance the production of 1-propanol and 1-butanol (Fig. 1). An E. coli strain (KS145) auxotrophic for L-isoleucine, leucine, and valine (
ilvI and
ilvB) was transformed with pSA63 (or other plasmids containing variants of cimA) and pSA55 (PLlacO1::kivd-ADH2 (2). The deletions of ilvI and ilvB (Fig. 1) were introduced for two reasons. First, the deletions eliminated the native substrate, 2- ketoisovalerate, for the leuABCD pathway, thus reducing the competitive substrate inhibition. Second, these deletions eliminated the production of 2-keto-3-methyl-valerate and 2-keto-4-methyl-pentanoate, which are competing substrates for Kivd. The strain expressing the wild-type cimA gene (KS145/pSA63/pSA55) produced 302 mg/liter 1-propanol and 18 mg/liter 1-butanol after 40 h (Fig. 5). KS145 with pSA55 only, where Kivd utilizes endogenous 2-keto acids, produced 40 mg/liter 1-propanol and 10 mg/liter 1-butanol under the same condition. KS145 without pSA55 and pSA63 produced neither 1-propanol nor 1-butanol (Fig. 5). Note that the yeast extract was added to the medium to boost the cell density. However, without glucose added to the medium the cells produce no alcohols (Fig. 5), indicating that these products were derived from glucose, but not from yeast extract.
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FIG. 5. 1-Propanol and 1-butanol production with the citramalate pathway. (Left panel) 1-Propanol production. (Right panel) 1-Butanol production in the same strain. The host is KS145, and overexpressed genes are indicated below the axis. Cultures were grown at 30°C in M9 medium containing 5 g/liter yeast extract with or without 72 g/liter glucose for 40 h.
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TABLE 3. 1-Propanol and 1-butanol production with the selected CimA mutants
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(Table 3). The production of 1-propanol and 1-butanol from the strain with CimA2
increased 2.4- and 1.6-fold, respectively, compared to the strain with CimA2. As a control, we also constructed a truncated version of the wild-type cimA (denoted WT
) without the acquired amino acid substitutions in CimA2. However, this construct showed diminished 1-propanol and 1-butanol production (Table 3). This result indicates that the truncated version of CimA requires other mutations (Ile47Val, His126Gln, and Thr204Ala) for enhanced activity.
The strains expressing the CimA3.1 to CimA3.9 mutants showed production levels of 1-propanol similar to those of the strain expressing CimA2
(Table 3). However, 1-butanol production increased compared to that in the strain with CimA2
(Table 3). The production of 1-propanol and 1-butanol from the strain expressing the CimA3.7 variant increased 9.2- and 21.9-fold, respectively, compared to that in the strain with wild-type CimA. In addition to the amino acid substitutions in CimA2
, CimA3.7 contains two new amino acid substitutions (Glu114Val and Leu238Ser).
Time profiles of alcohol production with CimA3.7.
Since CimA3.7 is the best alcohol producer, the production profiles of KS145/pSA55/pSA142 (containing cimA3.7) were characterized in shake flasks. Cell growth stopped after 10 h and remained stationary during alcohol production (Fig. 6A). The growth with IPTG was similar to that without IPTG, indicating that overexpression of this pathway had almost no effect on cell growth. Both 1-propanol and 1-butanol production increased in a linear fashion up to 40 h, after which the production rate appeared to decrease (Fig. 6B and C). This strain produced more than 3.5 g/liter 1-propanol and 524 mg/liter 1-butanol after 92 h. The formation of ethanol may be due to the native production by adhE or by the decarboxylation of pyruvate by Kivd (Fig. 6D). This result indicates that overexpression of the citramalate pathway coupled with 1-propanol and 1-butanol production can be tolerated by E. coli. The rate of glucose consumption decreased after 40 h, which is consistent with the alcohol production rates (Fig. 6E). Acetate and lactate are the major organic acids produced at a significant level (Fig. 6F).
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FIG. 6. 1-Propanol and 1-butanol production with CimA3.7. Time profiles of cell growth with IPTG (squares) and without IPTG (open circles) (A); 1-propanol (B), 1-butanol (C), and ethanol (D) production; glucose consumption (E); and organic acid production (acetate [diamonds], lactate [circles], formate [triangles]) (F) from KS145/pSA55/pSA142 (containing cimA3.7). Cultures were grown at 30°C in M9 medium containing 72 g/liter glucose and 5 g/liter yeast extract. OD600, optical density at 600 nm.
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FIG. 7. Sequence analysis of CimA3.7. (A) Structure of Mycobacterium tuberculosis LeuA. The residues in the active site and the bound 2-ketoisovalerate are colored blue and orange, respectively. The image on the left contains the regulator domain, while the image on the right does not. The residues corresponding to mutations in CimA3.7 are colored red. (B) Amino acid sequence alignment of CimA (M. jannaschii), LeuA (E. coli), and LeuA (M. tuberculosis). Multiple sequence alignment was carried out using ClustalW (17). Fully conserved residues are shaded. The residues in the active site are shown with asterisks. Residue mutations in CimA3.7 are labeled in red. Gaps in the sequence are shown with dashes.
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In the absence of actual crystallographic data, we cannot determine the specific mechanisms responsible for the observed increase activity of CimA3.7. However, the acquired mutations are not located near the catalytic center shown by homology alignment (Fig. 7B), suggesting these mutations may stabilize its active structure. It has been shown that thermophilic proteins have larger amino acid side chains, higher residue hydrophobicity, more charged amino acids, and fewer uncharged polar residues than mesophilic proteins (7). Twelve out of 18 substitutions identified in CimA3s result in the substitution of larger amino acids with smaller ones. Eight substitutions resulted in the substitution by amino acid residues with lower hydrophobicity. The replacement of native residues with uncharged polar residues was observed six times. Additionally, eight substitutions resulted in the replacement of a charged residue with a noncharged residue. Continued analysis of these mutations should provide further insight into the mechanism which leads to higher activity of CimA.
For further improvement of the alcohol production, the next step would be the strain modification by using a metabolic engineering approach. It is important to remove side products for achieving high yield. Ethanol, acetate, and lactate are the major side products in this strain (Fig. 6D and F). Obviation of the side products while maintaining metabolic balance is one key metabolic engineering objective for biofuel applications of this pathway.
We are grateful to Hyun-Jung Lim for experimental assistance and members of the Liao laboratory for discussion and comments on the manuscript.
Published ahead of print on 24 October 2008. ![]()
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