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dc.contributor.authorMartin, Collin H.
dc.contributor.authorWu, Danyi
dc.contributor.authorPrather, Kristala L. Jones
dc.date.accessioned2012-01-30T15:58:06Z
dc.date.available2012-01-30T15:58:06Z
dc.date.issued2010-01
dc.date.submitted2009-11
dc.identifier.issn0099-2240
dc.identifier.issn1098-5336
dc.identifier.urihttp://hdl.handle.net/1721.1/68703
dc.description.abstractEnzymes are powerful biocatalysts capable of performing specific chemical transformations under mild conditions, yet as catalysts they remain subject to the laws of thermodynamics, namely, that they cannot catalyze chemical reactions beyond equilibrium. Here we report the phenomenon and application of using extracytosolic enzymes and medium conditions, such as pH, to catalyze metabolic pathways beyond their intracellular catalytic limitations. This methodology, termed “integrated bioprocessing” because it integrates intracellular and extracytosolic catalysis, was applied to a lactonization reaction in Pseudomonas putida for the economical and high-titer biosynthesis of 4-valerolactone from the inexpensive and renewable source levulinic acid. Mutant paraoxonase I (PON1) was expressed in P. putida, shown to export from the cytosol in Escherichia coli and P. putida using an N-terminal sequence, and demonstrated to catalyze the extracytosolic and pH-dependent lactonization of 4-hydroxyvalerate to 4-valerolactone. With this production system, the titer of 4-valerolactone was enhanced substantially in acidic medium using extracytosolically expressed lactonase versus an intracellular lactonase: from <0.2 g liter−1 to 2.1 ± 0.4 g liter−1 at the shake flask scale. Based on these results, the production of 4-hydroxyvalerate and 4-valerolactone was examined in a 2-liter bioreactor, and titers of 27.1 g liter−1 and 8.2 g liter−1 for the two respective compounds were achieved. These results illustrate the utility of integrated bioprocessing as a strategy for enabling production from novel metabolic pathways and enhancing product titers.en_US
dc.description.sponsorshipSynthetic Biology Engineering Research Centeren_US
dc.description.sponsorshipNational Science Foundation (Grant Number EEC-0540879)en_US
dc.language.isoen_US
dc.publisherAmerican Society for Microbiologyen_US
dc.relation.isversionofhttp://dx.doi.org/10.1128/​AEM.01769-09en_US
dc.rightsCreative Commons Attribution-Noncommercial-Share Alike 3.0en_US
dc.rights.urihttp://creativecommons.org/licenses/by-nc-sa/3.0/en_US
dc.sourceProf. Prather via Erja Kajosaloen_US
dc.titleIntegrated Bioprocessing for the pH-Dependent Production of 4- Levulinate in Pseudomonas putida KT2440en_US
dc.typeArticleen_US
dc.identifier.citationMartin, Collin H., Danyi Wu and Kristala L. Jones Prather."Integrated Bioprocessing for the pH-Dependent Production of 4-Valerolactone from Levulinate in Pseudomonas putida KT2440." Applied and Environmental Microbiology, January 2010,76.2, p. 417-424.en_US
dc.contributor.departmentMassachusetts Institute of Technology. Department of Chemical Engineeringen_US
dc.contributor.approverPrather, Kristala L. Jones
dc.contributor.mitauthorPrather, Kristala L. Jones
dc.contributor.mitauthorMartin, Collin H.
dc.contributor.mitauthorWu, Danyi
dc.relation.journalApplied and Environmental Microbiologyen_US
dc.eprint.versionAuthor's final manuscripten_US
dc.identifier.pmid19915035
dc.type.urihttp://purl.org/eprint/type/JournalArticleen_US
eprint.statushttp://purl.org/eprint/status/PeerRevieweden_US
dspace.orderedauthorsMartin, Collin H.; Wu, Danyi; Prather, Kristala L. Jonesen_US
dc.identifier.orcidhttps://orcid.org/0000-0003-0437-3157
mit.licenseOPEN_ACCESS_POLICYen_US
mit.metadata.statusComplete


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