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Received September 14, 2016
Accepted December 20, 2016
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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대사공학으로 제작된 재조합 Klebsiella pneumoniae를 이용한 아세토인 생산

Acetoin Production Using Metabolically Engineered Klebsiella pneumoniae

고려대학교 화공생명공학과, 02841 서울특별시 성북구 안암로 145
Department of Chemical and Biological Engineering, Korea University, 145, Anam-ro, Seongbuk-gu, Seoul, 02841, Korea
mkoh@korea.ac.kr
Korean Chemical Engineering Research, April 2017, 55(2), 237-241(5), 10.9713/kcer.2017.55.2.237 Epub 31 March 2017
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Abstract

아세토인(acetoin)은 식품과 화학산업에서 플랫폼 물질로 이용되며 산업적으로 다양한 응용이 가능한 물질이다. 본 연구에서는 대사공학(metabolic engineering)을 이용하여 아세토인의 생산량이 증가한 재조합 Klebsiella pneumoniae를 구축하였다. 우선 2,3-부탄디올(2,3-butanediol)생산을 위해 제작되었던 재조합 K. pneumoniae (KMK-05)에서 두 가지 2,3-butanediol dehydrogenase (budC, dhaD)를 유전체에서 제거하여 아세토인 생산량을 늘리고, 전사인자 중 하나인 AcoK를 제거하여 아세토인을 분해하는 효소의 발현량을 줄였다. 그리고 NADH oxidase를 발현시켜 세포 내 산화 환원 균형(redox balance)을 맞춰 대사흐름을 개선하였다. 이렇게 대사공학을 통해 구축된 재조합 Klebsiella pneumoniae (KJW-03-nox)로 아세토인 생산량과 수율을 높였고, 36시간 동안의 유가식 배양을 진행하여 51 g/L의 아세토인 농도와 최대 생산성 2.6 g/L/h을 달성하였다.
Acetoin is variously applicable platform chemical in chemical and food industry. In this study, Klebsiella pneumoniae was engineered for acetoin production using metabolic engineering. From the recombinant Klebsiella pneumoniae (KMK-05) producing 2,3-butanediol, budC and dhaD genes encoding two 2,3-butanediol dehydrogenases were deleted to reduce 2,3-butanediol production. Furthermore, a transcriptional regulator, AcoK, was deleted to reduce the expression levels of acetoin degrading enzyme. Lastly, NADH oxidase was overexpressed for adjusting intracellular redox balance. The resulting strain (KJW-03-nox) produced considerable amount of acetoin, with concentration reaching 51 g/L with 2.6 g/L/h maximum productivity in 36 h fed-batch fermentation.

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