ITERATIVE PLATFORM FOR THE SYNTHESIS OF ALPHA FUNCTIONALIZED PRODUCTS
20230383319 · 2023-11-30
Assignee
Inventors
- Ramon Gonzalez (Tampa, FL, US)
- James M. Clomburg (Houston, TX, US)
- Seokjung Cheong (Emeryville, CA, US)
Cpc classification
C12N9/1217
CHEMISTRY; METALLURGY
C12Y103/01044
CHEMISTRY; METALLURGY
C12N9/0008
CHEMISTRY; METALLURGY
C12Y402/01017
CHEMISTRY; METALLURGY
C12Y203/01
CHEMISTRY; METALLURGY
C12N9/1029
CHEMISTRY; METALLURGY
C12Y101/01035
CHEMISTRY; METALLURGY
C12Y102/0101
CHEMISTRY; METALLURGY
International classification
C12N9/00
CHEMISTRY; METALLURGY
C12N9/12
CHEMISTRY; METALLURGY
Abstract
The use of microorganisms to make alpha-functionalized chemicals and fuels, (e.g. alpha-functionalized carboxylic acids, alcohols, hydrocarbons, amines, and their beta-, and omega-functionalized derivatives), by utilizing an iterative carbon chain elongation pathway that uses functionalized extender units. The core enzymes in the pathway include thiolase, dehydrogenase, dehydratase and reductase. Native or engineered thiolases catalyze the condensation of either unsubstituted or functionalized acyl-CoA primers with an alpha-functionalized acetyl-CoA as the extender unit to generate alpha-functionalized β-keto acyl-CoA. Dehydrogenase converts alpha-functionalized β-keto acyl-CoA to alpha-functionalized β-hydroxy acyl-CoA. Dehydratase converts alpha-functionalized β-hydroxy acyl-CoA to alpha-functionalized enoyl-CoA. Reductase converts alpha-functionalized enoyl-CoA to alpha-functionalized acyl-CoA. The platform can be operated in an iterative manner (i.e. multiple turns) by using the resulting alpha-functionalized acyl-CoA as primer and the aforementioned alpha-functionalized extender unit in subsequent turns of the cycle. Termination pathways acting on any of the four alpha-functionalized CoA thioester intermediates terminate the platform and generate various alpha-functionalized carboxylic acids, alcohols and amines with different β-reduction degree.
Claims
1. A genetically engineered bacteria, said bacteria comprising: a) an overexpressed acyl-CoA transferase enzyme that converts glycolate to glycolyl-CoA or propionate to propionyl-CoA and wherein said overexpressed acyl-CoA transferase enzyme is encoded by a Megasphaera elsdenii pct gene; b) an overexpressed thiolase enzyme that catalyzes a condensation of an acetyl-CoA primer or a propionyl-CoA primer with a propionyl-CoA extender or an acetyl-CoA primer with glycolyl-CoA extender to generate 2-methyl-3-ketobutyryl-CoA or 2-methyl-3-ketopentanoyl-CoA or 2-hydroxy-3-ketobutyryl-CoA, wherein said overexpressed thiolase enzyme is encoded by a gene(s) selected from a group consisting of Pseudomonas putida fadAx, Ralstonia eutropha bktB, Escherichia coli atoB, Escherichia coli yqeF, Escherichia coli fadA, Escherichia coli fadI, Pseudomonas sp. B13 catF, Escherichia coli paaJ, Rhodococcus opacus pcaF, Pseudomonas putida pcaF, Streptomyces sp. pcaF, Pseudomonas putida fadA, Ralstonia eutropha phaA, Acinetobacter sp. ADP1 dcaF, Clostridium acetobutylicum thlA, and Clostridium acetobutylicum thlB; c) an overexpressed 3-hydroxyacyl-CoA dehydrogenase enzyme that catalyzes a reduction of 2-methyl-3-ketobutyryl-CoA to 2-methyl-3-hydroxybutyryl-CoA or 2-methyl-3-ketopentanoyl-CoA to 2-methyl-3-hydroxypentanoyl-CoA or 2-hydroxy-3-ketobutyryl-CoA to 2,3-dihydroxybutyryl-CoA, wherein said overexpressed 3-hydroxyacyl-CoA dehydrogenase enzyme is encoded by a gene(s) selected from a group consisting of Pseudomonas putida fadB2x, Ralstonia eutropha phaB, Escherichia coli fadB, Escherichia coli fadJ, Escherichia coli paaH, Pseudomonas putida fadB, Acinetobacter sp. ADP1 dcaH, and Clostridium acetobutylicum hbd; d) an enoyl-CoA hydratase or a 3-hydroxyacyl-CoA dehydratase enzyme that catalyzes a dehydration of 2-methyl-3-hydroxybutyryl-CoA to 2-methyl-crotonoyl-CoA or 2-methyl-3-hydroxypentanoyl-CoA to 2-methyl-pentenoyl-CoA or 2,3-dihydroxybutyryl-CoA to 2-hydroxy-crotonoyl-CoA, wherein said overexpressed enoyl-CoA hydratase or 3-hydroxyacyl-CoA dehydratase enzyme is encoded by a gene(s) selected from a group consisting of Pseudomonas putida fadB1x, Escherichia coli fabA, Escherichia coli fabZ, Escherichia coli fadB, Escherichia coli fadJ, Escherichia coli paaF, Pseudomonas putida fadB, Acinetobacter sp. ADP1 dcaE, Clostridium acetobutylicum crt, and Aeromonas caviae phaJ; e) a trans-enoyl-CoA reductase or an enoyl-[acyl-carrier-protein]reductase enzyme that catalyzes a reduction of 2-methyl-crotonoyl-CoA to 2-methyl-butyryl-CoA or 2-methyl-pentenoyl-CoA to 2-methyl-pentanoyl-CoA or 2-hydroxy-crotonoyl-CoA to 2-hydroxy-butyryl-CoA, wherein said trans-enoyl-CoA reductase or enoyl-[acyl-carrier-protein] reductase enzyme is encoded by a gene(s) selected from a group consisting of Escherichia coli fabI, Euglena gracilis TER, Treponema denticola TER, Clostridium acetobutylicum TER, Enterococcus faecalis fabK, Bacillus subtilis fabL, and Vibrio cholerea fabV; f) a termination enzyme(s) able to use a substrate selected from any CoA thioester intermediate produced by enzymes b-e to make a product selected from 2-methyl-3-ketobutyrate, 2-methyl-3-hydroxybutyrate, 2-methyl-3-ketopentanoate, 2-methyl-3-hydroxypentanoate, 2-hydroxy-3-ketobutyrate, 2,3-dihydroxybutyrate, 2-methyl-crotonoate, 2-methyl-butyrate, 2-methyl-pentenoate, 2-methyl-pentanoate, 2-hydroxy-crotonoate, or 2-hydroxy-butyrate, wherein said termination enzyme(s) is selected from a group consisting of: i) a thioesterase encoded by a gene(s) selected from a group consisting of Escherichia coli tesA, Escherichia coli tesB, Escherichia coli yciA, Escherichia coli fadM, Escherichia coli ydiI, Escherichia coli ybgC, Escherichia coli paaI, Mus musculus acot8, Alcanivorax borkumensis tesB2, Fibrobacter succinogenes Fs2108, Prevotella ruminicola Pr655, Prevotella ruminicola Pr1687, and Lycopersicon hirsutum f. glabratum mks2; ii) an acyl-CoA transferase encoded by a gene(s) selected from a group consisting of Escherichia coli atoD, Escherichia coli scpC, Escherichia coli ydiF, Escherichia coli atoA, Escherichia coli atoD, Clostridium acetobutylicum ctfA, Clostridium acetobutylicum ctfB, Clostridium kluyveri cat2, Clostridium kluyveri cat1, Pseudomonas putida pcaI, Pseudomonas putida pcaJ, Megasphaera elsdenii pct, Acidaminococcus fermentans gctA, Acidaminococcus fermentans gctB, and Acetobacter aceti aarC; or iii) a phosphotransacylase encoded by a gene(s) selected from a group consisting of Clostridium acetobutylicum ptb, Enterococcus faecalis ptb, and Salmonella enterica pduL and a carboxylate kinase encoded by a gene(s) selected from a group consisting of Clostridium acetobutylicum buk, Enterococcus faecalis buk, and Salmonella enterica pduW.
2. A genetically engineered bacteria, said bacteria comprising: a. a Megasphaera elsdenii pct gene encoding acyl-CoA transferase enzyme that converts propionate to propionyl-CoA; b. a Pseudomonas putida fadAx gene encoding a thiolase that catalyzes the condensation of an acetyl-CoA primer or a propionyl-CoA primer with a propionyl-CoA extender to generate 2-methyl-3-ketobutyryl-CoA or 2-methyl-3-ketopentanoyl-CoA; c. a Pseudomonas putida fadB2x encoding a 3-hydroxyacyl-CoA dehydrogenase enzyme that catalyzes a reduction of 2-methyl-3-ketobutyryl-CoA to 2-methyl-3-hydroxybutyryl-CoA or 2-methyl-3-ketopentanoyl-CoA to 2-methyl-3-hydroxypentanoyl-CoA; d. a Pseudomonas putida fadB1x encoding an enoyl-CoA hydratase or a 3-hydroxyacyl-CoA dehydratase enzyme that catalyzes a dehydration of 2-methyl-3-hydroxybutyryl-CoA to 2-methyl-crotonoyl-CoA or 2-methyl-3-hydroxypentanoyl-CoA to 2-methyl-pentenoyl-CoA; e. an Escherichia coli fabI gene encoding a trans-enoyl-CoA reductase or an enoyl-[acyl-carrier-protein] reductase enzyme that catalyzes a reduction of 2-methyl-crotonoyl-CoA to 2-methyl-butyryl-CoA or 2-methyl-pentenoyl-CoA to 2-methyl-pentanoyl-CoA; f. an Escherichia coli ydiI gene encoding a thioesterase enzyme that catalyzes a conversion of 2-methyl-crotonoyl-CoA to 2-methyl-crotonoate or 2-methyl-butyryl-CoA to 2-methyl-butyrate or 2-methyl-pentenoyl-CoA to 2-methyl-pentenoate or 2-methyl-pentanoyl-CoA 2-methyl-pentanoate.
3. A genetically engineered bacteria, said bacteria comprising: a. a Megasphaera elsdenii pct gene encoding acyl-CoA transferase enzyme that converts propionate to propionyl-CoA; b. a Ralstonia eutropha bktB gene encoding a thiolase that catalyzes the condensation of an acetyl-CoA primer with glycolyl-CoA extender to generate 2-hydroxy-3-ketobutyryl-CoA; c. a Ralstonia eutropha phaB gene encoding a 3-hydroxyacyl-CoA dehydrogenase enzyme that catalyzes a reduction of 2-hydroxy-3-ketobutyryl-CoA to 2,3-dihydroxybutyryl-CoA; d. an endogenous Escherichia coli gene encoding a thioesterase enzyme that catalyzes the conversion of 2,3-dihydroxybutyryl-CoA to 2,3-dihydroxybutyrate.
4. A method of producing an alpha functionalized product, comprising growing the bacteria of claim 1 in a nutrient broth containing an alpha functionalized acid selected from propionic acid or glycolic acid under conditions such that said gene(s) are expressed, said microorganism producing an alpha functionalized product from said alpha-functionalized acid by reverse beta oxidation, wherein said alpha functionalized product is tiglic acid, 2-methylbutyric acid, 2-methylpentenoic acid, 2-methyl-2-pentenoic acid or 2-methylvaleric acid.
5. A method of making an alpha functionalized product, comprising growing the bacteria of claim 1 in a nutrient broth under conditions such that said gene(s) are expressed, said microorganism producing an alpha functionalized product from an alpha-functionalized acid by reverse beta oxidation, and isolating said alpha functionalized product.
6. The method of claim 5, wherein said nutrient broth is supplemented with said alpha-functionalized acid.
7. The method of claim 6, wherein said alpha-functionalized acid is propionic acid or glycolic acid.
8. The method of claim 7, wherein said alpha functionalized product is tiglic acid, 2-methylbutyric acid, 2-methylpentenoic acid, 2-methyl-2-pentenoic acid or 2-methylvaleric acid.
9. A method of producing an alpha functionalized product, comprising growing the bacteria of claim 2 in a nutrient broth containing an alpha functionalized acid selected from propionic acid or glycolic acid under conditions such that said gene(s) are expressed, said microorganism producing an alpha functionalized product from said alpha-functionalized acid by reverse beta oxidation, wherein said alpha functionalized product is selected from 2-methyl-butyrate, 2-methyl-pentanoate, 2-methyl-crotonoate, 2-methyl-pentenoate, and 2,3-dihydroxybutyrate.
10. A method of making an alpha functionalized product, comprising growing the bacteria of claim 2 in a nutrient broth under conditions such that said gene(s) are expressed, said microorganism producing an alpha functionalized product from an alpha-functionalized acid by reverse beta oxidation, and isolating said alpha functionalized product or a beta- or omega-functionalized derivative thereof.
11. The method of claim 10, wherein said nutrient broth is supplemented with said alpha-functionalized acid.
12. The method of claim 11, wherein said alpha-functionalized acid is propionic acid or glycolic acid.
13. The method of claim 12, wherein said alpha functionalized product is 2-methyl-butyrate, 2-methyl-pentanoate, 2-methyl-crotonoate, 2-methyl-pentenoate, and 2,3 -dihydroxybutyrate.
14. A method of producing an alpha functionalized product, comprising growing the bacteria of claim 3 in a nutrient broth containing an alpha functionalized acid selected from propionic acid or glycolic acid under conditions such that said gene(s) are expressed, said microorganism producing an alpha functionalized product from said alpha-functionalized acid by reverse beta oxidation, wherein said alpha functionalized product is selected from 2-methyl-butyrate, 2-methyl-pentanoate, 2-methyl-crotonoate, 2-methyl-pentenoate, and 2,3-dihydroxybutyrate.
15. A method of making an alpha functionalized product, comprising growing the bacteria of claim 3 in a nutrient broth under conditions such that said gene(s) are expressed, said microorganism producing an alpha functionalized product from an alpha-functionalized acid by reverse beta oxidation, and isolating said alpha functionalized product or a beta- or omega-functionalized derivative thereof.
16. The method of claim 15, wherein said nutrient broth is supplemented with said alpha-functionalized acid.
17. The method of claim 16, wherein said alpha-functionalized acid is propionic acid or glycolic acid.
18. The method of claim 17, wherein said alpha functionalized product 2-methyl-butyrate, 2-methyl-pentanoate, 2-methyl-crotonoate, 2-methyl-pentenoate, and 2,3-dihydroxybutyrate.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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DETAILED DESCRIPTION
[0078] This disclosure generally relates to the use of microorganisms to make alpha-functionalized chemicals and fuels, (e.g. alpha-functionalized carboxylic acids, alcohols, hydrocarbons, amines, and their beta-, and omega-functionalized derivatives), by utilizing a novel iterative carbon chain elongation pathway that uses functionalized extender units to grow a carbon chain by two carbon units.
[0079] The core enzymes in the pathway include thiolase, dehydrogenase, dehydratase and reductase. Native or engineered thiolases catalyze the condensation of either unsubstituted or functionalized acyl-CoA primers with an alpha-functionalized acetyl-CoA as the extender unit to generate alpha-functionalized β-keto acyl-CoA. Dehydrogenase converts alpha-functionalized β-keto acyl-CoA to alpha-functionalized β-hydroxy acyl-CoA. Dehydratase converts alpha-functionalized β-hydroxy acyl-CoA to alpha-functionalized enoyl-CoA. Reductase converts alpha-functionalized enoyl-CoA to alpha-functionalized acyl-CoA.
[0080] The platform can be operated in an iterative manner (i.e. multiple turns) by using the resulting alpha-functionalized acyl-CoA as primer and the aforementioned omega-functionalized extender unit in subsequent turns of the cycle. Various termination pathways (
[0081] Thioesterase or CoA transferase or phosphotransacylase+carboxylate kinase can terminate the platform by converting the alpha-functionalized acyl-CoAs to alpha-functionalized carboxylic acids. If alpha-functionalized carboxylic acids has keto group at the beta-site, it can then be converted to ketone through reactions by betα-keto acid decarboxylase. Acyl-CoA reductases can terminate the platform by converting the alpha-functionalized acyl-CoAs to alpha-functionalized aldehydes. Alpha-functionalized aldehydes can then be converted to alpha-functionalized alcohols and alpha-functionalized amines through reactions by alcohol dehydrogenase and transaminase respectively.
[0082] This disclosure also relates to a novel primary alcohol synthesis incorporating the proposed iterative platform using glycolyl-CoA (alpha-hydroxy acetyl-CoA) as the extender unit. When the platform uses glycolyl-CoA as the extender unit, it generates alpha-hydroxyacyl-CoA, which can be converted to primary alcohol by termination pathways selected from: a) 2-hydroxyacyl-CoA lyase (HACL) that converts alpha-hydroxyacyl-CoA to primary aldehyde with one less carbon and formyl-CoA, and alcohol dehydrogenase subsequently converts the primary aldehyde to primary alcohol; b) acid-forming termination enzyme selected from thioesterase, CoA transferase and phosphotransacylase+carboxylate kinase that converts alpha-hydroxyacyl-CoA to alpha-hydroxy acid, keto-dehydrogenase that converts alpha-hydroxy acid to alpha-keto acid, alpha-keto acid decarboxylase that converts alpha-keto acid to primary aldehyde with one less carbon and alcohol dehydrogenase subsequently converts the primary aldehyde to primary alcohol.
[0083] Many examples of thiolase enzymes which can potentially catalyze the non-decarboxylative condensation of an acyl-CoA primer and acetyl-CoA extender unit are provided herein and Table 1 provides several additional examples which can also serve as templates for engineered variants:
TABLE-US-00002 TABLE 1 Example Thiolase Enzymes (EC Number 2.3.1.-) Source organism and gene name Protein Accession Numbers E. coli atoB NP_416728.1 E. coli yqeF NP_417321.2 E. coli fadA YP_026272.1 E. coli fadl NP_416844.1 Streptomyces collinus fadA Q93C88 Ralstonia eutropha bktB AAC38322.1 Pseudomonas sp. Strain B13 catF AAL02407.1 E coli paaJ NP_415915.1 Pseudomonas putida pcaF AAA85138.1 Rhodococcus opacus pcaF YP_002778248.1 Streptomyces sp. pcaF AAD22035.1 Ralstonia eutropha phaA AEI80291.1 Clostridium acetobutylicum thlA AAC26023.1 Clostridium acetobutylicum thlB AAC26026.1
[0084] This technology takes the above thiolase initiated pathway one step further to make alpha functionalized products. The method entails developing a new pathway that is based on native or engineered thiolases capable of catalyzing the condensation of either unsubstituted or functionalized acyl-CoA primers with an omega-functionalized acetyl-CoA as the extender unit. This has been reported in neither the scientific, peer-reviewed literature nor the patent literature.
[0085] Materials that can be used with the invention include those in Tables 2-5 below.
TABLE-US-00003 TABLE 2 Activation enzymes EC Protein Num- Enzyme Source organism Accession Reaction Illustration bers names and gene name Numbers Carboxylic acid .fwdarw. Acyl- CoA (including acyl-CoA primer, and
TABLE-US-00004 TABLE 3 Reactions of the platform Protein EC Enzyme Source organism Accession Reaction Illustration Numbers names and gene name Numbers Acyl-CoA + α- functionalized acetyl-CoA .fwdarw. α- functionalized β-ketoacyl-CoA
TABLE-US-00005 TABLE 4 Termination Pathways EC Protein Num- Enzyme Source organism Accession Reaction Illustration bers names and gene name Numbers Acyl-CoA .fwdarw. Carboxylic acid
TABLE-US-00006 TABLE 5 Enzymes for derivatization of 2-hydroxy acid to primary alcohol EC Protein Num- Enzyme Source organism Accession Reaction Illustration bers names and gene name Numbers 2-hydroxy acid .fwdarw. α-keto acid
[0086] All strains used in this study are listed in Table 6. Gene deletions were performed using P1 phage transduction with single-gene knockout mutants from the National BioResource Project (NIG, Japan) as the specific deletion donor. The λDE3 prophage, carrying the T7 RNA polymerase gene and lacIq, was integrated into the chromosome through λDE3 lysogenization kit (Novagen, Darmstadt, Germany). All strains were stored in 32.5% glycerol stocks at −80° C. Plates were prepared using LB medium containing 1.5% agar, and appropriate antibiotics were included at the following concentrations: ampicillin (100 μg/mL), spectinomycin (50 μg/mL), kanamycin (50 μg/mL), and chloramphenicol (34 μg/mL).
[0087] All plasmids used in this study and oligonucleotides used in their construction are listed in Tables 6 and 7. Plasmid based gene overexpression was achieved by cloning the desired gene(s) into either pETDuet-1 or pCDFDuet-1 (Novagen, Darmstadt, Germany) digested with appropriate restriction enzymes using In-Fusion PCR cloning technology (Clontech Laboratories, Inc., Mountain View, CA). Cloning inserts were created via PCR of ORFs of interest from their respective genomic or codon-optimized DNA with Phusion polymerase (Thermo Scientific, Waltham, MA). E. coli genes were obtained from genomic DNA, while heterologous genes were synthesized by GenScript (Piscataway, NJ) or GeneArt (Life Technologies, Carlsbad, CA) with codon optimization except for bktB, phaB1, and pct, which were amplified from genomic DNA or cDNA of their source organisms. The resulting In-Fusion products were used to transform E. coli Stellar cells (Clontech Laboratories, Inc., Mountain View, CA) and PCR identified clones were confirmed by DNA sequencing.
TABLE-US-00007 TABLE 6 Strains and plasmids used in this study. Strain/plasmid Genotype E. coli Strains MG1655 F-λ-ilvG-rfb-50 rph-1 JC01 MG1655 ΔldhA::FRT ΔpoxB::FRT Δpta::FRT ΔadhE::FRT ΔfrdA::FRT JC01(DE3) JC01 with DE3, a λ prophage carrying the T7 RNA polymerase gene and lacl.sup.q JST06 JC01 ΔyciA::FRT ΔybgC::FRT Δydil::FRT ΔtesA::FRT ΔfadM::FRT ΔtesB::FRT JST06(DE3) JST06 with DE3, a λ prophage carrying the T7 RNA polymerase gene and lacl.sup.q MG1655(DE3) MG1655 with DE3, a λ prophage carrying the T7 RNA polymerase gene and lacl.sup.q MG1655(DE3) ΔglcD MG1655(DE3) ΔglcD::FRT BL21(DE3) F− ompT gal dem lon hsdS.sub.B(r.sub.B.sup.−m.sub.B.sup.−) λ(DE3 [lacl lacUV5-T7 gene 1 ind1 sam7 nin5]) [malB.sup.+].sub.K-12(λ.sup.S) S. cerevisiae strains INVSc1 MATa his3D1 leu2 trp1-289 ura3-52 MAT his3D1 leu2 trp1- 289 ura3-52 Plasmids pETDuet ColE1(pBR322) ori, lacl, T7lac, pETDuet-P1-fadB2x- ColE1 ori; Amp.sup.R; P.sub.T7lac-1: fadB2x-fadB1x fadB1x pETDuet-P1-fadB2x- ColE1 ori; Amp.sup.R; P.sub.T7lac-1: fadB2x-fadB1x P.sub.T7lac-2: ydil fadB1x-P2-ydil pETDuet-P1-bktB- ColE1 ori; Amp.sup.R; P.sub.T7lac-1: bktB-phaB1 phaB1 pETDuet-P1-bktB- ColE1 ori; Amp.sup.R; P.sub.T7lac-1: bktB-phaB1 P.sub.T7lac-2: phaJ phaB1-P2-phaJ pCDFDuet-1 CloDF13 ori, lacl, T7lac, Strep.sup.R pCDFDuet-P1-pct-fadAx CloDF13 ori; Strep.sup.R; P.sub.T7lac-1: pct-fadAx pCDFDuet-P1-pct- CloDF13 ori; Strep.sup.R; P.sub.T7lac-1: pct-fadAx P.sub.T7lac-2: fabl fadAx-P2-fabl pCDFDuet-P1-pct-P2- CloDF13 ori; Strep.sup.R; P.sub.T7lac-1: pct P.sub.T7lac-2: tdTer tdTer pCDFDuet-1-P1-ntH6- CloDF13 ori; Strep.sup.R; P.sub.T7lac-1: ntHis6-HACL1 HACL1 pYE260-HACL1 ColE1 ori; Amp.sup.R; P.sub.GAL1: ntHis6-HACL1
TABLE-US-00008 TABLE 7 Oligonucleotides used in this study for plasmid constructions Name SEQ ID Sequence pct-f1 1 5′-AGGAGATATACCATGAG AAAAGTAGAAATCATTAC-3′ pct-r1 2 5′-CGCCGAGCTCGAATTCT TATTTTTTCAGTCCCATGGG AC-3′ fabl-f1 3 5′-AAGGAGATATACATATG GGTTTTCTTTCCGGTAAG-3′ fabl-r1 4 5′-TTGAGATCTGCCATATG TTATTTCAGTTCGAGTTCGT TC-3′ fadAx-f1 5 5′-GAAAAAATAAGAATTTA AGGAGGAATAAACCATGACC CTGGCAAATGATCC-3′ fadAx-r1 6 5′-CGCCGAGCTCGAATTCT TAATACAGACATTCAACTGC C-3′ fadB2x-f1 7 5′-AGGAGATATACCATGCA TATCGCCAACAAACAC-3′ fadB2x-r1 8 5′-CGCCGAGCTCGAATTCT TATTTTGCTGCCATGCGCAG -3′ fadB1x-f1 9 5′-AGCAAAATAAGAATTTA AGGAGGAATAAACCATGGCC TTTGAAACCATTCTG-3′ fadB1x-r1 10 5′-CGCCGAGCTCGAATTCT TAGCGATCTTTAAACTGTGC -3′ ydil-f1 11 5′-AAGGAGATATACATATG ATATGGAAACGGAAAATCAC -3′ ydil-r1 12 5′-TTGAGATCTGCCATATG TCACAAAATGGCGGTCGTC- 3′ bktB-f1 13 5′-AGGAGATATACCATGAT GACGCGTGAAGTGGTAGT-3′ bktB-r1 14 5′-CGCCGAGCTCGAATTCT CAGATACGCTCGAAGATGG- 3′ phaB1-f1 15 5′-GCGTATCTGAGAATTAG GAGGCTCTCT ATGACTCAG CGCATTGCGTA phaB1-r1 16 5′-CGCCGAGCTCGAATTCT CAGCCCATGTGCAGGCC-3′ phaJ-f1 17 5′-AAGGAGATATACATATG TCGGCACAAAGCCTG-3′ phaJ-r1 18 5′-TTGAGATCTGCCATATG TTACGGCAGTTTCACCACC- 3′ HACL1-f1 19 5′-GCCAGGATCCGAATTct ATGCCGGACAGCAACTTC-3′ HACL1-r1 20 5′-CGCCGAGCTCGAATTc TTACATATTGCTACGGGTCA GC-3′
[0088] Fermentation medium and conditions: The minimal medium designed by Neidhardt et al. with 125 mM MOPS and Na.sub.2HPO.sub.4 in place of K.sub.2HPO.sub.4 (1.48 mM for fermentations in flasks; 2.8 mM for fermentations in bioreactors), supplemented with 20 g/L glycerol, 10 g/L tryptone, 5 g/L yeast extract, 100 μM FeSO.sub.4, 5 mM calcium pantothenate, 5 mM (NH.sub.4).sub.2SO.sub.4, and 30 mM NH.sub.4Cl was used for all fermentations unless otherwise stated. Neutralized 20 mM glycolic acid or propionic acid was supplemented as needed. Antibiotics (50 μg/mL carbenicillin and 50 μg/mL spectinomycin) were included when appropriate. All chemicals were obtained from Fisher Scientific Co. (Pittsburg, PA) and Sigma-Aldrich Co. (St. Louis, MO).
[0089] Unless otherwise stated, fermentations were performed in 25 mL Pyrex Erlenmeyer flasks (narrow mouth/heavy duty rim, Corning Inc., Corning, NY) filled with 20 mL fermentation medium and sealed with foam plugs filling the necks. A single colony of the desired strain was cultivated overnight (14-16 h) in LB medium with appropriate antibiotics and used as the inoculum (1%). After inoculation, flasks were incubated in a NBS I24 Benchtop Incubator Shaker (New Brunswick Scientific Co., Inc., Edison, NJ) at 200 rpm and 37° C., except fermentations supplemented with phenylacetic acid or isobutyric acid in which the temperature was 30° C. When optical density (550 nm, OD550) reached ˜0.3-0.5, 5 μM isopropyl β-d-1-thiogalactopyranoside (IPTG) was added for plasmid based gene expression in all cases except the following: 1 μM IPTG was used for adipic acid production from glycerol without succinic acid supplementation and 10 μM IPTG was used during production of ω-phenylalkanoic acids. For induction of controlled chromosomal expression constructs, 0.1 mM cumate and 15 ng/mL anhydrotetracycline were also added when appropriate. Flasks were then incubated under the same conditions for 48 h post-induction unless otherwise stated.
[0090] Additional fermentations were conducted in a SixFors multi-fermentation system (Infors HT, Bottmingen, Switzerland) with an air flow rate of 2 N L/hr, independent control of temperature (37° C.), pH (controlled at 7.0 with NaOH and H.sub.2SO.sub.4), and stirrer speed (720 rpm). Tiglic acid fermentations used the previously described fermentation media with 30 g/L glycerol, the inclusion of 5 μM sodium selenite, and 5 μM IPTG. Propionic acid (20 mM) was added at 0, 24, and 48 h. Pre-cultures were grown in 25 mL flasks as described above, incubated for 4 h post-induction, and used for inoculation as described above.
[0091] Fermentations with glycolyl-CoA as a primer were conducted in 250 mL Erlenmeyer Flasks filled with 50 mL LB media supplemented with 10 g/L glucose and appropriate antibiotics. The cultivation of inoculum was same as above but 2% inoculation was used. After inoculation, cells were cultivated at 30° C. and 250 rpm in a NBS 124 Benchtop Incubator Shaker until an optical density of ˜0.8 was reached, at which point IPTG (0.1 mM) and neutralized glycolic acid (40 mM) were added. Flasks were then incubated under the same conditions for 96 h post induction.
[0092] GC sample preparation: Sample preparation was conducted as follows: 2 mL culture supernatant samples were transferred to 5 mL glass vials (Fisher Scientific Co., Fair Lawn, NJ, USA) and 80 μL of 50% H.sub.2SO.sub.4 and 340 μL of 30% NaCl solution were added for pH and ionic strength adjustment, respectively. Tridecanoic acid (final concentration 50 mg/L) was added as internal standard and 2 mL of hexane-MTBE (1:1) added for extraction. The bottles were sealed with Teflonlined septa (Fisher Scientific Co., Fair Lawn, NJ, USA), secured with caps, and rotated at 60 rpm for 120 min. The samples were then centrifuged for 2 min at 2,375×g to separate the aqueous and organic layers. 1 mL of the dry organic layer was transferred into a 2 mL borosilicate glass vial, dried under N.sub.2, and re-suspended in 1000 μL of pyridine. After vortexing, 100 μL of BSTFA (N,O-bis(trimethylsilyl)trifluoroacetamide) was added, the samples were heated at 70° C. for 30 min, dried under N.sub.2 and re-suspended in 1 mL hexane for analysis.
[0093] GC-MS metabolite identification: Except identifications of 2,3-dihydroxybutyric acid, metabolite identification was conducted via GC-MS in an Agilent 7890A GC system (Agilent Technologies, Santa Clara, CA), equipped with a 5975C inert XL mass selective detector (Agilent) and Rxi-5Sil column (0.25 mm internal diameter, 0.10 μm film thickness, 30 m length; Restek, Bellefonte, PA). The sample injection amount was 2 μL with 40:1 split ratio. The injector and detector were maintained at 280° C. The column temperature was held initially at 35° C. for 1 min and increased to 200° C. at the rate of 6° C./min, then to 270° C. at the rate of 30° C./min. That final temperature was maintained for 1 min before cooling back to initial temperature. The carrier gas was helium (2.6 mL/min, Matheson Tri-Gas, Longmont, CO).
[0094] Identification of 2,3-dihydroxybyturic acid was conducted by the Baylor College of Medicine Analyte Center (bcm.edu/research/centers/analyte, Houston, TX). An Agilent 6890 GC system (Agilent Technologies, Santa Clara, CA), equipped with a 5973 mass selective detector (Agilent Technologies) and HP-5 ms column (Agilent Technologies) was used. Sample extraction was conducted using Agilent Chem Elut liquid extraction columns (Agilent Technologies) according to manufacturer protocols.
[0095] HPLC metabolite quantification: The concentration of products were determined via ion-exclusion HPLC using a Shimadzu Prominence SIL 20 system (Shimadzu Scientific Instruments, Inc., Columbia, MD) equipped with an HPX-87H organic acid column (Bio-Rad, Hercules, CA) with operating conditions to optimize peak separation (0.3 ml/min flow rate, 30 mM H.sub.2SO.sub.4 mobile phase, column temperature 42° C.).
[0096] In vitro enzyme assay: Purified HACL1 was tested for its native catabolic activity by assessing its ability to cleave 2-hydroxyhexadecanoyl-CoA to pentadecanal and formyl-CoA. Enzyme assays were performed in 50 mM tris-HCl pH 7.5, 0.8 mM MgCl.sub.2, 0.02 mM TPP, 6.6 μM BSA, and 0.3 mM 2-hydroxyhexadecanoyl-CoA. The assay mixtures were incubated for one hour at 37° C., after which the presence of pentadecanal was assessed by extraction with hexane and analysis by GC-FID.
[0097] 2-hydroxyhexadecanoyl-CoA was prepared by the n-hydroxysuccinimide method. In summary, the n-hydroxysuccinimide ester of 2-hydroxyhexadecanoic acid is prepared by reacting n-hydroxysuccinimide with the acid in the presence of dicyclohexylcarbodiimide. The product was filtered and purified by recrystallization from methanol to give pure n-hydroxysuccinimide ester of 2-hydroxyhexadecanoic acid. The ester was reacted with CoA-SH in presence of thioglycolic acid to give 2-hydroxyhexadecanoyl-CoA. The 2-hydroxyhexadecanoyl-CoA was purified precipitation using perchloric acid, filtration, and washing the filtrate with perchloric acid, diethyl ether, and acetone.
[0098] For specific activity assays (reported in μmol substrate/mg protein/min) these supernatant fractions were utilized and protein concentration was established using the Bradford Reagent (Thermo Sci.) using BSA as the protein standard.
[0099] Enzyme purification: A plasmid containing the codon optimized gene encoding human HIS-tagged HACL1 was constructed as described. The resulting construct was transformed into S. cerevisiae InvSC1 (Life Tech.). The resulting strain was cultured in 50 mL of SC-URA media containing 2% glucose at 30° C. for 24 hours. The cells were pelleted and the required amount of cells were used to inoculate a 250 mL culture volume of SC-URA media containing 0.2% galactose, 1 mM MgCl.sub.2, and 0.1 mM thiamine to 0.4 OD600. After 20 hours incubation with shaking at 30° C., the cells were pelleted and saved.
[0100] When needed, the cell pellets were resuspended to an OD600 of approximately 100 in a buffer containing 50 mM potassium phosphate pH 7.4, 0.1 mM thiamine pyrophosphate, 1 mM MgCl.sub.2, 0.5 mM AEBSF, 10 mM imidazole, and 250 units of Benzonase nuclease. To the cell suspension, approximately equal volumes of 425-600 μm glass beads were added. Cells were broken in four cycles of 30 seconds of vortexing at 3000 rpm followed by 30 seconds on ice. The glass beads and cell debris were pelleted by centrifugation and supernatant containing the cell extract was collected. The HIS-tagged HACL1 was purified from the cell extract using Talon Metal Affinity Resin as described above, with the only modification being the resin bed volume and all subsequent washes were halved. The eluate was collected in two 500 μL fractions.
[0101] Expression and purification of the desired protein can be confirmed by running cell pellet sample and eluate on SDS-PAGE.
[0102] We demonstrated several cases of the iterative system can synthesize alpha-functionalized small molecules through the use of alpha-functionalized forms of acetyl-CoA as the extender unit. One case used of propionyl-CoA as the extender unit. To implement this, P. putida FadAx (thiolase), FadB2x (HACD), FadB1x (ECH), and E. coli FabI (ECR) were used with Pct for activation of exogenous propionic acid. Expression in JC01(DE3) resulted in the production of 2-methylbutyric acid (75 mg/L) and tiglic acid (573 mg/L) (
[0103] Interestingly, 2-methylpentanoic acid (49 mg/L) and (E)-2-methyl-2-pentenoic acid (84 mg/L) were also synthesized, as the result of propionyl-CoA serving as both the primer and the extender unit. Products resulting from non-functionalized extender units (acetyl-CoA) with acetyl-CoA or propionyl-CoA priming were also observed, demonstrating the nonspecific activity of the thiolase (and subsequent β-reduction enzymes). This represents a potential area for further improvement through the selection and engineering of a thiolase with maximal specificity for the desired condensation. Additional alpha-functionalization was demonstrated with glycolyl-CoA (i.e. α-hydroxylated acetyl-CoA) as the extender unit, which with acetyl-CoA priming supported the synthesis of 2,3-dihydroxybutyric acid (
[0104] The ability of the alpha-functionalization system to support high product titers was investigated by improving tiglic acid production. Omission of ECR and manipulation of the termination pathway through deletion of native thioesterases and controlled overexpression of YdiI, a thioesterase previously shown to act effectively on α,β-unsaturated enoyl-CoAs, resulted in further improvement, from 573 mg/L to 1.39 g/L (
[0105] The host strains and plasmids used for production of above products are summarized in Table 8.
TABLE-US-00009 TABLE 8 Host strains and plasmids enabling alpha-functionalized small molecule synthesis with listed primer/extender unit combinations Host strain Plasmid 1 Plasmid 2 Primer Extender unit Product JC01(DE3) pETDuet-P1- pCDFDuet-P1- Acetyl-CoA Propionyl-CoA 2- fadB2x-fadB1x pct-fadAx-P2-fabl methylbutyric acid Tiglic acid Propionyl-CoA Propionyl-CoA 2- methylpentanoic acid (E)-2-methyl-2- pentenoic acid JC01(DE3) pETDuet-P1- pCDFDuet-P1- Acetyl-CoA Propionyl-CoA Tiglic acid fadB2x-fadB1x pct-fadAx JST06(DE3) pETDuet-P1- pCDFDuet-P1- Acetyl-CoA Propionyl-CoA N.A. fadB2x-fadB1x pct-fadAx JST06(DE3) pETDuet-P1- pCDFDuet-P1- Acetyl-CoA Propionyl-CoA Tiglic acid fadB2x-fadB1x- pct-fadAx P2-ydil Acetyl-CoA Glycolyl-CoA 2,3- Acetyl-CoA Glycolyl-CoA 2,3- dihydroxybutyric dihydroxybutyric acid acid
[0106] We also successfully expressed Homo sapiens 2-hydroxyacyl-CoA lyase HACL1 in Saccharomyces cerevisiae and Escherichia coli (
[0107] We believe that, pathway and process optimization, in line with industrial biotechnology approaches, can further improve performance for a specific target product, as the underlying carbon and energy efficiency enables the feasibility of further advancing product titer, rate, and yield. Important areas include generating and balancing pools of priming and extender units and optimization of required pathway enzymes for a given target product. The former can exploit previously developed pathways for primers and extender units, whereas the latter includes identifying and engineering enzymes that may be flux limiting due to suboptimal enzyme specificity or activity. These approaches will be continually aided by developments in protein and metabolic engineering and synthetic and systems biology.
[0108] The above experiments are repeated in Bacillus subtilis. The same genes can be used, especially since Bacillus has no significant codon bias. A protease-deficient strain like WB800N is preferably used for greater stability of heterologous protein. The E. coli-B. subtilis shuttle vector pMTLBS72 exhibiting full structural stability can be used to move the genes easily to a more suitable vector for Bacillus. Alternatively, two vectors pHT01 and pHT43 allow high-level expression of recombinant proteins within the cytoplasm. As yet another alternative, plasmids using the theta-mode of replication such as those derived from the natural plasmids pAMβ1 and pBS72 can be used. Several other suitable expression systems are available. Since the FAS genes are ubiquitous, the invention is predicted to function in Bacillus.
[0109] The above experiments are repeated in yeast. The same genes can be used, but it may be preferred to accommodate codon bias. Several yeast E. coli shuttle vectors are available for ease of the experiments. Since the FAS genes are ubiquitous, the invention is predicted to function in yeast, especially since yeasts are already available with exogenous functional TE genes and the reverse beta oxidation pathway has also been made to run in yeast.
[0110] Each of the following is incorporated by reference herein in its entirety for all purposes: [0111] U.S. 20130316413 Reverse beta oxidation pathway. [0112] 62/140,628 Bioconversion of short-chain hydrocarbons to fuels and chemicals, Mar. 31, 2015. [0113] WO2015112988 Type II fatty acid synthesis enzymes in reverse beta-oxidation, Jan. 26, 2015 and 61/932,057, Jan. 27, 2014. [0114] 62/069,850 Synthetic pathway for biosynthesis from 1-carbon compounds, Oct. 29, 2014. [0115] 61/531/911, Sep. 7, 2011; 61/440,192, Feb. 7, 2011, U.S. 20140273110, WO2013036812 Functionalized carboxylic acids and alcohols by reverse fatty acid oxidation.
[0116] Heath, R.J. & Rock, C.O. The Claisen condensation in biology. Nat. Prod. Rep. 19, 581-596 (2002). [0117] Haapalainen, A. M., et al., The thiolase superfamily: condensing enzymes with diverse reaction specificities. Trends in Biochemical Sciences 31, 64-71 (2006). [0118] Jiang, C., et al., Divergent evolution of the thiolase superfamily and chalcone synthase family. Molecular Phylogenetics and Evolution 49, 691-701 (2008). [0119] Choi, K. H., et al., β-Ketoacyl-Acyl Carrier Protein Synthase III (FabH) Is a Determining Factor in Branched-Chain Fatty Acid Biosynthesis. J. Bacteriol. 182, 365-370 (2000). [0120] Pfleger, B. F., et al., Metabolic engineering strategies for microbial synthesis of oleochemicals. Metab. Eng. 29, 1-11 (2015). [0121] Dellomonaco, C., et al., Engineered reversal of the β-oxidation cycle for the synthesis of fuels and chemicals. Nature 476, 355-359 (2011). [0122] Clomburg, J. M., et al., Synthetic Biology Approach to Engineer a Functional Reversal of the β-Oxidation Cycle. ACS Synthetic Biology 1, 541-554 (2012). [0123] Vick, J. E. et al. Escherichia coli enoyl-acyl carrier protein reductase (FabI) supports efficient operation of a functional reversal of the β-oxidation cycle. Appl. Environ. Microbiol. 81, 1406-1416 (2015). [0124] Cheong, S., Clomburg, J. M. and Gonzalez, R.* (2016). Energy- and carbon-efficient synthesis of functionalized small molecules in bacteria using non-decarboxylative Claisen condensation reactions. Nat. Biotechnol. 34 (5): doi:10.1038/nbt.3505.
[0125] The following claims are provided to add additional clarity to this disclosure. Future applications claiming priority to this application may or may not include the following claims, and may include claims broader, narrower, or entirely different from the following claims. Further, any detail from any claim may be combined with any other detail from another claim, even if not yet so combined.