KR101417146B1 - 이소프레노이드의 생산 방법 - Google Patents
이소프레노이드의 생산 방법 Download PDFInfo
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- KR101417146B1 KR101417146B1 KR1020087029580A KR20087029580A KR101417146B1 KR 101417146 B1 KR101417146 B1 KR 101417146B1 KR 1020087029580 A KR1020087029580 A KR 1020087029580A KR 20087029580 A KR20087029580 A KR 20087029580A KR 101417146 B1 KR101417146 B1 KR 101417146B1
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- mevalonate
- isoprenoid
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Abstract
Description
Claims (43)
- (a) 이소펜테닐 피로포스페이트를 생성하는 메발로네이트 경로의 하나 이상의 효소를 암호화하는 이종 핵산을 포함하는 다수의 박테리아 또는 진균 숙주 세포를 얻는 단계로서, 하나 이상의 효소의 발현은 하나 이상의 이종 전사 조절 인자의 제어 하에 있고, 상기 메발로네이트 경로는(ⅰ) 아세토아세틸-CoA를 아세틸-CoA와 축합시켜 HMG-CoA를 형성하는 효소;(ⅱ) HMG-CoA를 메발로네이트로 전환시키는 효소;(ⅲ) 메발로네이트를 메발로네이트 5-포스페이트로 인산화하는 효소;(ⅳ) 메발로네이트 5-포스페이트를 메발로네이트 5-피로포스페이트로 전환시키는 효소; 및(ⅴ) 메발로네이트 5-피로포스페이트를 이소펜테닐 피로포스페이트로 전환시키는 효소를 포함하는 것인 단계; 및(b) 배지가 박테리아 또는 진균 숙주 세포에 대해 최대 비 생장률의 75% 이하를 제공하도록 탄소 공급원이 제한되는 배지에서 박테리아 또는 진균 숙주 세포를 배양하는 단계로서, 상기 최대 비 생장률은 박테리아 또는 진균 숙주 세포의 성장에 대한 최적 온도 및 영양소가 과량 존재하는 배지 중에서 박테리아 또는 진균 숙주 세포를 배양함으로써 얻어지는 생장률인 단계를 포함하는 이소프레노이드의 생산 방법.
- 제1항에 있어서, 하나 이상의 이종 전사 조절 인자는 유도가능한 것인 생산 방법.
- 제1항에 있어서, 메발로네이트 경로 효소는 단일 전사 조절 인자의 제어 하에 있는 것인 생산 방법.
- 제1항에 있어서, 메발로네이트 경로 효소는 복수의 전사 조절 인자의 제어 하에 있는 것인 생산 방법.
- 제1항에 있어서, 숙주 세포는 메발로네이트 경로의 효소 모두를 암호화하는 다수의 이종 핵산을 포함하는 것인 생산 방법.
- 제1항에 있어서, 박테리아 세포는 이. 콜라이(E. coli)인 생산 방법.
- 제1항에 있어서, 이종 핵산은 내인성 메발로네이트 경로를 가지는 진균으로부터 유래하는 메발로네이트 경로 효소를 암호화하는 핵산 서열을 포함하는 것인 생산 방법.
- 제1항에 있어서, 숙주 세포는 에스. 세레비지아에(S. cerevisiae)인 생산 방법.
- 제1항에 있어서, 이종 핵산은 내인성 메발로네이트 경로를 가지는 박테리아로부터 유래하는 메발로네이트 경로 효소를 암호화하는 핵산 서열을 포함하는 것인 생산 방법.
- 제9항에 있어서, 박테리아는 엔테로코커스(Enterococcus), 슈도모나스(Pseudomonas) 및 스타필로코커스(Staphylococcus)로부터 선택되는 속에 속하는 것인 생산 방법.
- 제1항에 있어서, 이종 핵산은 아세틸-CoA 티올라제, HMG-CoA 합성 효소, HMG-CoA 환원 효소 및 메발로네이트 키나제로부터 선택되는 메발로네이트 경로 효소를 암호화하는 핵산 서열을 포함하는 것인 생산 방법.
- 제1항에 있어서, 이종 핵산은 제II군 HMG 환원 효소를 암호화하는 핵산 서열을 포함하는 것인 생산 방법.
- 제1항에 있어서, 숙주 세포를 영양소와 온도 둘 다가 숙주 세포에 대해 최대 비 생장률을 제공하는 수준보다 낮은 수준으로 유지되는 배지 중에서 배양하는 것인 생산 방법.
- 제1항에 있어서, 배지의 온도는 최적 온도보다 2∼20℃ 이상 낮은 것인 생산 방법.
- 제14항에 있어서, 숙주 세포를 최적 온도보다 5℃ 이상 낮은 온도에서 배양하는 것인 생산 방법.
- 제14항에 있어서, 배지의 온도는 최적 온도보다 10℃ 이상 낮은 것인 생산 방법.
- 제1항에 있어서, 배지는 최대 비 생장률의 60% 이하를 제공하는 것인 생산 방법.
- 제1항에 있어서, 배지는 최대 비 생장률의 50% 이하를 제공하는 것인 생산 방법.
- 제1항에 있어서, 배지는 최대 비 생장률의 40% 이하를 제공하는 것인 생산 방법.
- 제1항에 있어서, 배지는 최대 비 생장률의 25% 이하를 제공하는 것인 생산 방법.
- 제1항에 있어서, 배지는 최대 비 생장률의 75∼10%를 제공하는 것인 생산 방법.
- 제1항에 있어서, 배지는 질소가 제한되는 것인 생산 방법.
- 제1항에 있어서, 이소프레노이드가 배지 1 ℓ당 10 g보다 많은 양으로 생산되는 것인 생산 방법.
- 제1항에 있어서, 이소프레노이드가 건조 세포 중량 1 그램당 50 ㎎보다 많은 양으로 생산되는 것인 생산 방법.
- 제23항 또는 제24항에 있어서, 상기 이소프레노이드의 양이 150 시간보다 적은 시간 내에 생산되는 것인 생산 방법.
- 제23항 또는 제24항에 있어서, 상기 이소프레노이드의 양이 96 시간보다 적은 시간 내에 생산되는 것인 생산 방법.
- 제23항 또는 제24항에 있어서, 상기 이소프레노이드의 양이 72 시간보다 적은 시간 내에 생산되는 것인 생산 방법.
- 제1항에 있어서, 이소프레노이드는 헤미테르펜, 모노테르펜, 디테르펜, 트리테르펜, 테트라테르펜, 세스퀴테르펜 및 폴리테르펜으로 이루어진 군으로부터 선택되는 것인 생산 방법.
- 제1항에 있어서, 이소프레노이드는 세스퀴테르펜인 생산 방법.
- 제1항에 있어서, 이소프레노이드는 C5-C20 이소프레노이드인 생산 방법.
- 제1항에 있어서, 이소프레노이드는 아비에타디엔, 아모르파디엔, 카렌, α-파네센, β-파네센, 파네솔, 게라니올, 게라닐게라니올, 이소프렌, 리날룰, 리모넨, 미르신, 네롤리돌, 오시멘, 패출롤, β-피넨, 사비넨, γ-테르피넨, 테르핀덴 및 발렌센으로 이루어진 군으로부터 선택되는 것인 생산 방법.
- 제1항에 있어서, 영양소는 탄소 공급원 및 질소 공급원을 포함하는 것인 생산 방법.
- 제29항에 있어서, 세스퀴테르펜은 α-파네센인 생산 방법.
- 제29항에 있어서, 세스퀴테르펜은 β-파네센인 생산 방법.
- 제29항에 있어서, 세스퀴테르펜은 아모르파디엔인 생산 방법.
- 제29항에 있어서, 세스퀴테르펜은 파네솔인 생산 방법.
- 제29항에 있어서, 세스퀴테르펜은 네롤리돌인 생산 방법.
- 제29항에 있어서, 세스퀴테르펜은 패출롤인 생산 방법.
- 제29항에 있어서, 세스퀴테르펜은 발렌센인 생산 방법.
- 제1항에 있어서, 상기 하나 이상의 효소는 박테리아 효소인 생산 방법.
- 제1항에 있어서, 상기 하나 이상의 효소는 진균 효소인 생산 방법.
- 삭제
- 삭제
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