KR101542563B1 - 융합 파트너와 샤페론을 이용한 수용성 유기인화합물 분해효소의 제조방법 - Google Patents
융합 파트너와 샤페론을 이용한 수용성 유기인화합물 분해효소의 제조방법 Download PDFInfo
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- KR101542563B1 KR101542563B1 KR1020130059272A KR20130059272A KR101542563B1 KR 101542563 B1 KR101542563 B1 KR 101542563B1 KR 1020130059272 A KR1020130059272 A KR 1020130059272A KR 20130059272 A KR20130059272 A KR 20130059272A KR 101542563 B1 KR101542563 B1 KR 101542563B1
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- ala
- gly
- glu
- val
- lys
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Abstract
본 발명은 수용성 발현이 증가된 유기인화합물 가수분해효소(Organophosphorus hydrolase, OPH)의 제조방법에 관한 것으로, 더욱 상세하게는 플라보박테리움 종(Flavobacterium sp.) 유래의 OPH를 수용성이 강한 융합 파트너(fusion partner)와 결합된 형태로 대장균에서 발현시키는 것을 특징으로 하는 유기인화합물 가수분해효소의 제조방법에 관한 것이다.
본 발명에 따르면, 통상적으로 숙주세포에서 불용성 상태로 발현되는 재조합 유기인화합물 분해효소를 수용성 고활성 상태로 제조할 수 있어, 상업적으로 유용한 유기인화합물 분해효소 대량생산에 유용하다.
본 발명에 따르면, 통상적으로 숙주세포에서 불용성 상태로 발현되는 재조합 유기인화합물 분해효소를 수용성 고활성 상태로 제조할 수 있어, 상업적으로 유용한 유기인화합물 분해효소 대량생산에 유용하다.
Description
본 발명은 수용성 발현이 증가된 유기인화합물 가수분해효소(Organophosphorus hydrolase, OPH)의 제조방법에 관한 것으로, 더욱 상세하게는 플라보박테리움 종(Flavobacterium sp.) 유래의 OPH를 수용성이 강한 융합 파트너(fusion partner)와 결합된 형태로 대장균에서 발현시키는 것을 특징으로 하는 유기인화합물 가수분해효소의 제조방법에 관한 것이다.
유기인 화합물은 알킬 또는 아릴기 R과 인원자 P가 직접 결합되어 있는 화합물이다. 유기인 화합물은 파라옥손(Paraoxon), 말라티온(Malathion), 디아지논(Diazinon), 트리부포스(Tribufos)등의 살충제와 제초제로 산업적으로 널리 이용되고 있다. 또한, 군사적으로 사린(Sarin), 소만(Soman), 타분(Tabun) 등의 화학무기로써 신경작용제로 이용된다. 이러한 화합물들이 인간의 체내에 유입되면 아세틸콜린에스터라제(acertylcholinesterase)의 활성 저해작용을 일으켜서 근육성 진통을 포함하는 만성적인 합병증 유발 및 생명에 위협을 주는 물질로 밝혀졌다.
유기인 화합물의 생물학적 처리는 효소를 이용하는 방법이 있다. OPH는 P-O, P-F, P-CN, P-S등의 다양한 인산 에스테르(phosphorus-ester) 결합을 가수분해 할 수 있다. 유기인 화합물을 기질로 하여 다양한 생물체에서 OPH가 확인되었다. 그 중 플라보박테리움 종 유래의 OPH가 넓은 기질 특이성과 높은 가수분해 활성 때문에 꾸준히 연구되어 왔다. 플라보박테리움 종 유래의 OPH는 1989년에 유전자 염기서열이 확인 되었다(W W Mulbry. et al., Journal of Bacteriology, 6740-6746, 1989). 그러나, OPH의 불용성은 재조합 대장균을 이용한 OPH의 대량생산에 어렵게 한다. OPH의 수용성 발현을 위한 여러 시도가 있었으나, 대량생산을 위한 충분한 효율은 아니었다.
유전공학 기법을 이용하여 미생물로부터 목적 단백질을 대량생산하는 발현 방법은 다양하게 개발되어 왔다. 이러한 방법 중에서 목적 단백질을 융합형태로 발현시킬 경우, 결합 파트너의 강한 수용성으로 인해 목적 단백질의 수용성 발현을 유도 할 수 있으며, 숙주효소에 의해 쉽게 분해되는 외래 단백질을 숙주 내에서 안정화 시킬 수도 있다. 또한, 발현된 생산물의 정제를 용이하게 하므로, 생산물을 효과적으로 얻을 수 있으며, 발현된 생산물을 숙주내의 특정부위, 예를 들면 페리플라즘(periplasm)이나 세포벽 혹은 배양액으로 분비케 할 수도 있다. 융합 파트너로는 베타-갈락토시다제(β-galactosidase), CAT(chloramphenicol acetyltransferase), GST(glutathione S transferase) 및 MBP(maltose binding protein) 등의 단백질이 사용된다. 그러나, 이들 융합 파트너의 결합이 모든 불용성 단백질의 수용성 발현을 보장하지는 않는다. 또한, 수용성 발현을 성공하여도 목적 단백질의 활성을 잃어버리는 경우도 많다.
재조합 대장균에서 목적 단백질의 생산시 불용성의 형태(inclusion body)를 형성하거나 단백질 분해효소(protease)에 의해 분해되는 경우는 발현된 단백질이 정확하게 접힘(folding)되지 않을 시에 나타나는 대표적인 현상이다. 샤페론(chaperone)은 단백질이 고유의 특성을 가지는 입체구조를 갖도록 도와주는 단백질이다. 열 충격 단백질(heat shock protein)이 대표적인 샤페론이며, 이 샤페론과 목적 단백질을 동시 발현은 기존의 불용성 응집체를 형성하고 있던 단백질의 가용화하여 회수 효율을 높일 수가 있다.
이에, 본 발병자들은 유기인산 화합물 분해에 이용되는 OPH를 수용성 상태로 제조하기 위하여 예의 노력한 결과, OPH의 최적 융합 단백질과 샤페론을 동시 발현하는 경우, 고활성의 수용성 OPH를 제조할 수 있다는 것을 확인하고 본 발명을 완성하게 되었다.
본 발명의 목적은 유기인산 화합물 분해에 이용되는 OPH를 수용성 상태로 제조하는 방법을 제공하는 데 있다.
상기 목적을 달성하기 위하여, 본 발명은 (a) 에놀라아제(enolase), 글루카나아제(glucanase), DnaK 및 MBP(maltose binding Protein)로 구성된 군에서 선택되는 수용성 융합파트너를 코딩하는 유전자와 유기인 화합물 분해효소를 코딩하는 유전자가 융합단백질로 발현되도록 삽입된 재조합 벡터 및 GroES/EL 샤페론을 함유하는 재조합 벡터로 형질전환된 미생물을 배양하여 수용성 융합파트너와 유기인 화합물 분해효소의 융합단백질을 생산하는 단계; 및 (b) 상기 생산된 수용성 융합파트너와 유기인 화합물 분해효소의 융합단백질을 수득하는 단계를 포함하는 수용성 유기인화합물 분해효소의 제조방법을 제공한다.
본 발명에 따르면, 통상적으로 숙주세포에서 불용성 상태로 발현되는 재조합 유기인화합물 분해효소를 수용성 고활성 상태로 제조할 수 있어, 상업적으로 유용한 유기인화합물 분해효소 대량생산에 유용하다.
도 1은 본 발명에서 사용한 7종의 재조합 벡터의 구조를 나타낸 것이다.
도 2는 수용성 융합 단백질의 결합없이 재조합 대장균에서 OPH의 발현 후에 SDS-PAGE를 수행 결과이다(T: total fraction, S: soluble fraction, P: insoluble fraction).
도 3은 다양한 수용성 융합 단백질과 결합된 OPH를 재조합 대장균에서 발현한 후에 SDS-PAGE를 수행 결과이다(T: total fraction, S: soluble fraction, P: insoluble fraction).
도 4는 융합 단백질과 결합하거나 그렇지 않은 OPH의 활성을 비교한 그래프이다.
도 5는 MBP와 결합된 OPH를 샤페론과 동시 발현 후 활성을 비교한 그래프이다.
도 2는 수용성 융합 단백질의 결합없이 재조합 대장균에서 OPH의 발현 후에 SDS-PAGE를 수행 결과이다(T: total fraction, S: soluble fraction, P: insoluble fraction).
도 3은 다양한 수용성 융합 단백질과 결합된 OPH를 재조합 대장균에서 발현한 후에 SDS-PAGE를 수행 결과이다(T: total fraction, S: soluble fraction, P: insoluble fraction).
도 4는 융합 단백질과 결합하거나 그렇지 않은 OPH의 활성을 비교한 그래프이다.
도 5는 MBP와 결합된 OPH를 샤페론과 동시 발현 후 활성을 비교한 그래프이다.
달리 정의되지 않는 한, 본 명세서에서 사용된 모든 기술적 및 과학적 용어들은 본 발명이 속하는 기술분야에서 숙련된 전문가에 의해서 통상적으로 이해되는 것과 동일한 의미를 갖는다. 일반적으로, 본 명세서에서 사용된 명명법 및 이하에 기술하는 실험 방법은 본 기술분야에서 잘 알려져 있고 통상적으로 사용되는 것이다.
일 관점에서, 본 발명은 (a) 에놀라아제(enolase), 글루카나아제(glucanase), DnaK 및 MBP(maltose binding Protein)로 구성된 군에서 선택되는 수용성 융합파트너를 코딩하는 유전자와 유기인 화합물 분해효소를 코딩하는 유전자가 융합단백질로 발현되도록 삽입된 재조합 벡터 및 GroES/EL 샤페론을 함유하는 재조합 벡터로 형질전환된 미생물을 배양하여 수용성 융합파트너와 유기인 화합물 분해효소의 융합단백질을 생산하는 단계; 및 (b) 상기 생산된 수용성 융합파트너와 유기인 화합물 분해효소의 융합단백질을 수득하는 단계를 포함하는 수용성 유기인화합물 분해효소의 제조방법에 관한 것이다.
본 발명에 있어서, "유기인산 화합물 가수분해 효소 (organophosphorus hydrolase, OPH)"는 유기인산 화합물 분해 효소 (organophosphosphate-degrading enzyme) 또는 포스포트리에스터라제(phosphotriestrase)라고 불리우며, 슈도모나스 디미누타 MG(Pseudomonas diminuta MG) 및 플라보박테리움 종 (Flavobacterium sp. strainATCC 27551)으로부터 분리된 효소이다.
본 발명에 있어서, 상기 유기인 화합물 분해효소는 플라보박테리움 종 유래인 것을 사용하는 것이 바람직하나 이에 한정되는 것은 아니다.
본 발명의 상기 유기인 화합물 분해효소는 서열번호 1의 아미노산 서열을 가지는 것을 특징으로 할 수 있다.
본 발명에 있어서, "유기인산 화합물 (organophosphorus compounds)"은 신경계에서 아세틸콜린 에스터라제를 억제하여, 신경 기능을 차차 손상시키고 결국 죽음에 이르게 하는 이유로 매우 독성인 물질로 알려져 있어, 산업적으로 이러한 화합물들이 포함되어 있는 살충제, 농약 등의 제거 방법에 관한 여러 연구가 이루어지고 있다.
이러한 유기인산 화합물의 예시로써, 파라옥손(paraoxon), 파라티온(parathion), 아자메티포스(azametiphos), 아진포스(azinphos), 벤술리드(bensulide), 말라옥손(malaoxon), 말리티온(malathion), 헤프테토포스(heptenophos), 디클로보스(dichlorvos), 디알리포스(dialifos), 디아지논(diazinon), 디클로펜티온(dichlofenthion), 디메토에이트(dimethoate), 디메틸빈포스(dimethylvinphos), 디옥사벤조포스(dioxabenzofos), 디설포톤(disulfoton), 데메톤 에스(demethon S), 에디펜포스(edifenphos), 에테폰(ethephon), 에티온(ethion), 에토프로포스(ethoprophos), 클로펜빈포스(chlorfenvinphos), 클로피리포스(chlorpyrifos), 페니트로티온(fenitrothion), 펜티온(fenthion), 포노포스(fonofos), 포모티온(formothion), 헵테노포스(heptenophos), 이프로벤포스(iprobenfos), 이사조포스(isazofos), 이속사티온(isoxathion), 메카밤(mecarbam), 메타미도포스(methamidophos), 메티다티온(methidathion), 모노크로토포스(monocrotophos), 날레드(naled), 오메토에이트(omethoate), 폭심(phoxim), 피림포스(pirimphos), 프로페노포스(profenofos), 프로파포스(propaphos), 프로티오포스(prothiofos), 피라클로포스(pyraclofos), 피라조포스(pyrazophos), 피리다펜티온(pyridaphenthion), 퀴날포스(quinalphos), 터부포스(terbufos), 테트라클로빈포스(tetrachlorvinphos), 티오메톤(thiometon), 톨클로포스(tolclofos), 트리아조포스(triazophos), 트리클로폰(trichlorphon), 바미도티온(vamidothion) 및 코우마포스(coumaphos) 등이 있다.
본 발명에서 수용성 융합파트너로 사용되는 가용화 단백질은효율적으로 단백질 응집을 예방하고, 손상된 단백질의 리폴딩(refolding)을 초래한다. 이들 수용성 융합파트너 단백질은 융합파트너를 가용화 시키는 것이 아니며, 융합되는 단백질의 특성에 따라, 융합단백질의 가용화 여부 및 정도가 달라진다.
본 발명의 일 양태에서는 OPH 단백질의 수용성 융합 파트너로서, 페리틴(ferritin) GroEs, DnaK, HSP31, 글루카네이즈(glucanase), 에놀레이즈 (enolase), MBP 등을 사용하여, 융합단백질을 제조하고, 상기 융합단백질의 가용성을 확인하였으며, 그 결과, 페리틴(ferritin) GroEs 및 HSP31의 경우는 OPH 단백질을 충분한 정도로 가용화 시키지 못하였다.
따라서, 본 발명의 유기인 화합물 분해효소(OPH)의 수용성 융합파트너로는 에놀라아제(enolase), 글루카나아제(glucanase), DnaK, MBP(maltose binding Protein)를 사용할 수 있으며, 상기 에놀라아제(enolase), 글루카나아제(glucanase), DnaK 및 MBP(maltose binding Protein)는 각각 서열번호 2, 서열번호 3, 서열번호 4 및 서열번호 5의 아미노산 서열을 가지는 것을 특징으로 할 수 있다.
본 발명에서 제작된 재조합 벡터의 골격벡터로는 pRSET, pMAL(c2X), pET28a(+), pACE로 등을 사용할 수 있다.
본 발명에 있어서, 상기 형질전환된 미생물은 대장균일 수 있으나 이에 한정되는 것은 아니다.
특정한 경우에, 샤페론의 과발현이 응집하기 쉬운 단백질의 가용성 수율을 증가시키는 것으로 발견되었다 ([Baneyx, F., Curr. Opin. Biotech. 10:411-421, 1999). 이 프로세스는 미리 형성된 재조합 봉입체의 용해를 수반하는 것으로 나타나지 않았지만, 새롭게 합성된 단백질 사슬의 개선된 폴딩에 관련된다. 예를 들어, Nishihara 등은 groESL 및 dnaJK/grpE를 세포질에서 동시발현시켜 재조합 Cryj2 (일본 삼나무 꽃가루의 알레르겐)의 안정성을 개선시켰다 ([Nishihara K. et al., Appl. Environ. Microbiol. 64:1694, 1998). 그러나, 이러한 샤페론의 세포내 농도 증가와 관련된 이로운 효과는 과잉생산된 단백질의 성질에 고도로 의존적인 것으로 여겨지고, 성공은 결코 보장되지 않는다.
따라서, 본 발명의 일양태에서는 샤페론 단백질로 알려진 dnaK-danJ-grpE, groES-groEL, dnaK-danJ-grpE, groES-groEL-tig 및 tig를 상기 OPH-MBP 융합단백질과 동시발현시켜, OPH의 활성을 확인하였으며, 그 결과, groES-groEL(groES/EL)의 경우 OPH-MBP 융합단백질의 활성이 4배 이상 증가하는 것을 확인하였다.
본 발명에서, 상기 GroES/GroEL은 각각 서열번호 6 및 서열번호 7의 아미노산 서열을 가지는 것을 특징으로 할 수 있다.
다른 관점에서, 본 발명은 (a) MBP(maltose binding Protein)를 코딩하는 유전자와 유기인 화합물 분해효소를 코딩하는 유전자가 융합단백질로 발현되도록 삽입된 재조합 벡터 및 GroES/EL 샤페론을 코딩하는 유전자를 함유하는 재조합 벡터로 형질전환된 미생물을 배양하여 수용성 융합파트너와 유기인 화합물 분해효소의 융합단백질을 생성하는 단계; 및 (b) 상기 생성된 수용성 융합파트너와 유기인 화합물 분해효소의 융합단백질을 수득하는 단계.를 포함하는 수용성 유기인화합물 분해효소의 제조방법에 관한 것이다.
본 발명의 일 양태에서, MBP를 융합파트너로하여 OPH를 융합단백질 형태로 생산할 경우, 융합되지 않은 OPHqhek 5배 이상의 유기인화합물 분해 활성을 나타내었다 (도 3).
본 발명의 다른 양태에서는 GroES/EL 샤페론을 MBP-OPH 융합단백질과 함께 발현시킬 경우, 단독으로 MBP-OPH 융합단백질만 발현시킨 경우에 비하여 유기인화합물 분해 활성이 4배 증가하였다 (도 4).
본 발명에서, "벡터 (vector)"는 적합한 숙주 내에서 DNA를 발현 시킬 수 [0048] 있는 적합한 조절 서열에 작동가능하게 연결된 DNA 서열을 함유하는 DNA 제조물을 의미한다. 벡터는 플라스미드, 파지 입자 또는 간단하게 잠재적 게놈 삽입물 일 수 있다. 적당한 숙주로 형질전환되면, 벡터는 숙주게놈과 무관하게 복제하고 기능할 수 있거나, 또는 일부경우에 게놈 그 자체에 통합될 수 있다. 플라스미드가 현재 벡터의 가장 통상적으로 사용되는 형태이므로, 본 발명의 명세서에서 "플라스미드(plasmid)" 및 "벡터(vector)"는 때로 상호교환적으로 사용된다.
본 발명의 목적상, 플라스미드 벡터를 이용하는 것이 바람직하다. 이러한 목적에 사용될 수 있는 전형적인 플라스미드 벡터는 (a) 숙주세포당 수백개의 플라스미드벡터를 포함하도록 복제가 효율적으로 이루어지도록하는 복제 개시점, (b) 플라스미드 벡터로 형질전환된 숙주세포가 선발될 수 있도록 하는 항생제 내성 유전자 및 (c) 외래 DNA 절편이 삽입될 수 있도록 하는 제한효소 절단부위를 포함하는 구조를 지니고 있다. 적절한 제한효소 절단부위가 존재하지 않을지라도, 통상의 방법에 따른 합성 올리고뉴클레오타이드어댑터(oligonucleotideadaptor) 또는 링커(linker)를 사용하면 벡터와 외래 DNA를 용이하게 라이게이션(ligation) 할 수 있다.
아울러, 상기 유전자는 다른 핵산 서열과 기능적 관계로 배치될 때 "작동가능하게 연결(operably linked)"된다. 이것은 적절한 분자(예를 들면, 전사 활성화 단백질)가 조절 서열(들)에 결합될 때 유전자 발현을 가능하게 하는 방식으로 연결된 유전자 및 조절 서열(들) 일 수 있다. 예를 들면, 전서열(pre-sequence) 또는 분비리더(leader)에 대한 DNA는 폴리펩타이드의 분비에 참여하는 전단백질로서 발현되는 경우 폴리펩타이드에 대한 DNA에 작동가능하게 연결되고; 프로모터 또는 인핸서는 서열의 전사에 영향을 끼치는 경우 코딩서열에 작동가능하게 연결되거나; 또는 리보좀 결합 부위는 서열의 전사에 영향을 끼치는 경우 코딩 서열에 작동가능하게 연결되거나; 또는 리보좀 결합 부위는 번역을 용이하게 하도록 배치되는 경우 코딩 서열에 작동가능하게 연결된다.
일반적으로 "작동가능하게 연결된"은 연결된 DNA 서열이 접촉하고, 또한 분비 리더의 경우 접촉하고 리딩 프레임 내에 존재하는 것을 의미한다. 그러나, 인핸서(enhancer)는 접촉할 필요가 없다. 이들 서열의 연결은 편리한 제한 효소 부위에서 라이게이션 (연결)에 의해 수행된다. 그러한 부위가 존재하지 않는 경우, 통상의 방법에 따른 합성 올리고뉴클레오티드 어댑터(oligonucleotide adaptor) 또는 링커(linker)를 사용한다.
물론 모든 벡터가 본 발명의 DNA 서열을 발현하는데 모두 동등하게 기능을 발휘하지는 않고, 마찬가지로 모든 숙주가 동일한 발현 시스템에 대해 동일하게 기능을 발휘하지는 않는다. 그러나, 당업자라면 과도한 실험적 부담없이 본 발명의 범위를 벗어나지 않는 상태에서, 다른 여러 벡터, 발현 조절 서열 및 숙주 중에서 적절한 선택하여 적용할 수 있다. 예를 들어, 벡터를 선택함에 있어서는 숙주를 고려하여야 하는데, 이는 벡터가 그 안에서 복제되어야만 하기 때문이고, 벡터의 복제 수, 복제 수를 조절할 수 있는 능력 및 당해 벡터에 의해 코딩되는 다른 단백질, 예를 들어 항생제 마커의 발현도 또한 고려되어야만 한다.
앞서 설명한 라이게이션 후에, 재조합 벡터는 적절한 숙주세포로 형질전환되어야 한다. 여기서, 선호되는 숙주세포는 원핵세포이고, 적합한 원핵 숙주세포는 대장균일 수 있고, 예컨대, E. coli JM109, E. coli DH5α, E.coli JM101, E. coli K12, E. coli W3110, E. coli X1776, E. coli XL1-Blue(Stratagene, 미국), E. coli B,E. coli B21(DE3), E. coli TOP10 등을 포함한다. FMB101, NM522, NM538 및 NM539와 같은 E. coli 균주 및 다른 원핵생물의 종(species) 및 속(genera)등이 또한 사용될 수 있다. 전술한 E. coli에 덧붙여, 아그로박테리움 A4와 같은 아그로박테리움 속 균주, 바실루스 섭틸리스(Bacillus subtilis)와 같은 바실리(bacilli), 살모넬라타이피뮤리움(Salmonella typhimurium) 또는 세라티아 마르게센스(Serratia marcescens)와 같은 또 다른 장내세균 및 다양한 슈도모나스(Pseudomonas) 속 균주가 숙주세포로서 이용될 수 있다. 또한, 효모 및 곰팡이와 같은 진핵세포를 숙주로 사용하는 것도 가능하다.
상기 형질전환된 재조합 미생물은 임의의 형질전환 방법에 따라 제조할 수 있다. 본 발명의 "형질전환(transformation)"은 DNA를 숙주로 도입하여 DNA가 염색체의 인자로서 또는 염색체 통합완성에 의해 복제 가능하게 되는 것으로 외부의 DNA를 세포 내로 도입하여 인위적으로 유전적인 변화를 일으키는 현상을 의미한다. 일반적으로 형질전환방법에는, 특히, 원형질세포의 형질전환은 Sambrook 등의 'Molecular Cloning' 저서에서 1.82섹션에 기술된 칼슘 클로라이드를 이용한 heat shock 방법을 사용해서 용이하게 달성될 수 있다. 선택적으로, 전기천공법(electroporaton, (Neumann et al., EMBO J., 1:841, 1982)), 인산칼슘(CaPO4) 침전, 염화칼슘(CaCl2)침전, 미세주입법(microinjection), 초산 리튬-DMSO법 등이 이용가능하다. 또한, 본 발명에서 상기 유전자를 숙주세포의 염색체상에 삽입하는 방법으로는 통상적으로 알려진 유전자조작방법을 사용할 수 있으며, 일예로는 레트로바이러스 벡터, 아데노바이러스 벡터, 아데노-연관 바이러스 벡터, 헤르페스 심플렉스 바이러스벡터, 폭스바이러스 벡터, 렌티바이러스 벡터 또는 비바이러스성 벡터를 이용하는 방법을 들 수 있다.
상기 형질전환된 재조합 미생물의 배양은 널리 공지된 방법에 따라서 수행되고, 배양 온도 및 시간, 배지의 pH 등의 조건은 적절하게 조절될 수 있다.
상기 배양된 재조합 미생물로부터의 유기인산 화합물 가수분해효소 변이체의 회수는 통상적인 생화학 분리기술, 예를 들어 단백질 침전제에 의한 처리(염석법), 원심분리, 초음파 파쇄, 한외여과, 투석법, 분자체 크로마토그래피(겔여과), 흡착크로마토그래피, 이온교환 크로마토그래피, 친화도 크로마토그래피 등의 각종 크로마토그래피 등을 이용할 수 있으며, 통상적으로 순도가 높은 단백질을 분리하기 위하여 이들을 조합하여 이용할수 있다.
이하, 실시예를 통하여 본 발명을 더욱 상세히 설명하고자 한다. 이들 실시예는 오로지 본 발명을 예시하기 위한 것으로서, 본 발명의 범위가 이들 실시예에 의해 제한되는 것으로 해석되지는 않는 것은 당업계에서 통상의 지식을 가진 자에게 있어서 자명할 것이다. 특히, 하기 실시예에서는 유기인산 화합물로 파라옥손에 대한 활성 증가를 확인하였으나, 이를 포함한 다른 유기인산 화합물에 대해서도 본 발명의 변이체가 뛰어난 분해활성을 가지는 것은 당업자에게 자명할 것이다.
실시예 1: 수용성 융합 단백질을 포함하는 발현벡터의 제조
수용성 융합 단백질 7종이 포함된 각각의 벡터를 제조하였다. 수용성 파트너 6종은 대장균(E. coli K-12) 유래의 단백질로 ferritin, GroES, DnaK, Hsp31, glucanase, enolase이며 pRSET(Invitrogen사) 벡터에 클로닝하였다. 나머지 1종은 MBP 결합되어 상업적으로 판매되는 pMAL(NEB사) 벡터를 사용하였다. 대장균을 LB(1.0% 트립톤, 0.5% 효모추출물, 1.0% 염화나트륨인) 배지에 37℃에서 밤새 배양하였다. 대장균 세포로부터 게놈 DNA 500㎍을 분리(Genomic DNA extraction kit; RBC사)하였다. 분리된 게놈 DNA를 주형으로 각각의 프라이머를 이용하여 다음과 같이 PCR을 수행하였다. 서열번호 7과 8은 ferritin, 서열번호 9와 10은 GroES, 서열번호 11과 12는 DnaK, 서열번호 13과 14는 Hsp31, 서열번호 15와 16은 glucanase, 서열번호 17과 18은 enolase를 위한 프라이머로 각각 사용하였다. Ferritin, GroES, DnaK의 PCR 산물은 제한효소 BamHI과 EcoRI을 처리하였고, Hsp31, glucanse, enolase의 PCR 산물은 제한효소 BamHI과 KpnI을 처리하였다. pRSET 벡터는 각각 PCR 산물에 맞는 제한효소를 처리하였고, 수용성 융합 단백질들을 라이게이션(Ligation)하여 융합 벡터들을 제작하였다.
벡터 | 융합 단백질 | 융합 단백질 서열번호 |
pRSET | Ferritin | 서열번호8: aaaaggatccatgctgaaaccagaaatgat 서열번호9: aaaagaattcgttttgtgtgtcgagggtag |
GroES | 서열번호10: aaaaggatccatgaatattcgtccattgca 서열번호11: aaaagaattccgcttcaacaattgccagaa |
|
DnaK | 서열번호12: aaaaggatccatgaaatccagaaaatggta 서열번호13: aaaagaattcttttttgtctttgacttctt |
|
Hsp31 | 서열번호14: aaaaggatccatgactgttcaaacaagtaa 서열번호15: aaaaggtaccacccgcgtaagctgccagca |
|
Glucanase | 서열번호16: aaaaggatccatggctgaaattaccgcatc 서열번호17: aaaaggtaccagactgcttggacatcgcag |
|
Enolase | 서열번호18: aaaaggatccatgtccaaaatcgtaaaaat 서열번호19: aaaaggtacctgcctggcctttgatctct |
|
pMAL | MBP | - |
실시예 2: OPH 유전자를 함유한 재조합 벡터 및 재조합 미생물의 제조
플라보박테리움(Flavobacterium sp KCTC2480)을 조성이 0.05% 질산칼슘, 0.2% 제2인산나트륨, 0.5% 펩톤, 1.5% 설탕, 0.05% 제일황산철7수염인 배지에 30℃에서 24시간 배양하였다. 상기 세포로부터 게놈 DNA 500㎍을 분리(Genomic DNA extraction kit; RBC사)하였다. 상기 분리된 게놈 DNA를 주형으로 하고 서열번호 19와 서열번호 20의 프라이머를 이용하여 PCR을 수행하여 mature OPH PCR 산물은 제한효소 EcoRI과 HindIII로 처리하였고, 서열번호 21와 서열번호 20의 프라이머를 이용하여 PCR 산물은 제한효소 KpnI과 HindIII로 처리하였다. 상기 실시예 1에서 제작된 융합 벡터들과 상업적으로 판매되는 pMAL 벡터에 각각에 맞는 동일 제한효소를 처리하고, OPH 유전자를 라이게이션하여 융합 OPH 벡터 7종을 제작하였다. 또한, 대조군으로 융합 단백질이 없는 OPH를 발현하기 위해 pET-28a(+) 벡터(Novagen사)를 제한효소 EcoRI과 HindIII로 처리하고 OPH 유전자를 라이게이션하였다(도 1). 제작된 8종의 벡터를 대장균 BL21(DE3)에 42℃ 열충격 방법으로 형질전환 시켰다. 형질전환된 대장균은 수용성 융합 OPH 생산을 위한 숙주로 사용되었다.
서열번호 20: aaaagaattcatgtcgatcggcacaggcgatcg
서열번호 21: aaaaaagctttcatgacgcccgcaaggtcg
서열번호 22: aaaaggtaccatgtcgatcggcacaggcgatcg
실시예 3: 재조합 융합 OPH의 생산 및 수용성 발현 확인
상기의 형질전환체를 이용하여 OPH를 생산하였다. 각각의 재조합 대장균 BL21(DE3)의 단일 콜로니를 3 ml LB 배지에 접종 후 5 시간 종 배양하였다. 100 ml의 LB 배지에 종 배양액을 2% 접종하고 30℃, 200 rpm으로 배양하였다. 600 nm의 파장에서 흡광도가 0.5일 때 최종 농도가 1 mM 인 IPTG를 처리한 후 6시간 동안 배양하였다. 초음파분쇄기(VibraCell사)로 형질전환된 재조합 균주를 파쇄하고, 후에 원심분리로 단백질을 soluble fraction과 insoluble fraction으로 나누어 SDS-PAGE 전기영동법으로 분석하였다.
SDS-PAGE (sodium dodecyl sulfate-polyacrylamide gel electrophoresis)는 세퍼레이팅 젤이 아크릴아미드 (acrylamide)의 농도가 12%가 되도록 만들었고, 스태킹 젤은 아크릴아미드의 농도가 8%가 되도록 만들었다. SDS-PAGE 완충액은 25 mM Tris-base, 192 mM 글리신, 0.1% SDS, pH 8.3을 사용하였다. 희석 시료는 5ㅧ샘플 버퍼 (60mM Tris-HCl pH 6.8, 25% 글리세롤, 2% SDS, 14.4mM 2-머캅토에탄올, 0.1% 브로모페놀 블루)와 혼합하여 100℃, 5분간 열처리하여 사용하였다. 전기영동장치는 Bio-Rad, Mini-ProteanⅡ apparatus를 이용하였다. 아크릴아미드 겔에서 전개된 시료는 CBB(Coomassie Brilliant Blue) 염색 수행 후, 탈색하였다.
도 2에 나타난 바와 같이, 수용성 단백질과 결합하지 않고, OPH 단독으로 재조합 발현시 대다수가 불용성 단백질을 나타내는 insoluble fraction에서 OPH 밴드를 확인할 수 있었다.
도 3에 나타난 바와 같이, ferritin, GroES와의 OPH 융합은 수용성 발현을 나타내는 가용성 분획(soluble fraction)에서 단백질 밴드가 나타나지 않았다. Hsp31과의 OPH 융합은 약한 수용성 발현을 보였다. 나머지 enolase, glucanase, DnaK, MBP는 강한 수용성 발현을 나타내었다.
실시예 4: 융합 OPH의 활성 확인
유기인산 화합물의 한 종류인 paraoxon(Supelco사)을 DMSO(dimethyl sulfoxide, Sigma사) 에 녹여 10 mg/ml 농도가 되도록 만들었다. 299μl CHES(2-(cyclohexylamino)ethanesulfonic acid, Sigma사) buffer (pH 8.5), 1μl paraoxon(10 mg/ml), 100μl OPH 용액(배양된 각 세포를 파쇄후 원심분리하여 회수한 상층액)을 혼합하여 50℃에서 10 분간 반응하였다.
반응 후 300μl 10% TCA(trichloroacetic acid, Sigma사)와 300 ul 10% sodium carbonate(Sigma사)를 첨가하여 반응을 정지시켰다. 효소 활성은 415 nm에서의 흡광도에서 유리된 P-니트로페놀의 농도를 확인하였다. OPH 1 unit는 상기 조건에서 1분당 1 μmol의 P-니트로페놀을 유리시키는 효소의 양으로 결정하였다.
상기 구축된 8종의 발현 벡터를 가지는 대장균의 soluble fraction에서 생산된 OPH의 활성을 도 4에 나타내었다. MBP와 융합된 OPH(MBP+OPH)의 활성이 가장 좋았으며, 그 활성도는 대조군인 융합되지 않은 OPH보다 5배 이상이었다.
실시예 5: 융합 OPH와 샤페론 단백질의 동시발현
샤페론 단백질의 동시발현을 위하여, 샤페론 플라스미드 세트(TaKaRa사)를 사용하였다. 이 세트의 구성은 표 2에 나타내었다. 상기 가장 좋은 활성을 보인 MBP 융합 OPH 벡터와 표 2에 제시된 5종의 벡터를 5가지 조합으로 대장균 BL21(DE3)에 42℃ 열충격 방법으로 형질전환시켰다. 상기 IPTG에 의한 OPH 발현과 동시에 샤페론을 발현시키기 위하여 araB 프로모터를 이용하는 벡터는 LB 배지에 1 mg/ml 농도로 arabinose를 첨가하였고, Pzt1 프로모터를 이용하는 벡터는 LB 배지에 1 ng/ml 농도로 tetracyclin을 첨가하였다.
그 결과, 도 5에 나타난 바와 같이, 가용성 분획(soluble fraction) 내 5종의 샤페론 조합과 발현된 OPH의 활성 비교에서, pGro7 벡터와 동시 발현된 MBP 융합 OPH의 활성이 4배 증가되었다.
Plasmid | Chaperon | Promoter | Inducer |
pG-KJE8 | dnaK-danJ-grpE groES-groEL |
araB Pzt1 |
L-Arabinose Tetracyclin |
pGro7 | groES-groEL | araB | L-Arabinose |
pKJE7 | dnaK-danJ-grpE | araB | L-Arabinose |
pG-Tf2 | groES-groEL-tig | Pzt1 | Tetracyclin |
pTf16 | tig | araB | L-Arabinose |
이상으로 본 발명 내용의 특정한 부분을 상세히 기술하였는바, 당업계의 통상의 지식을 가진 자에게 있어서 이러한 구체적 기술은 단지 바람직한 실시의 일예일 뿐이며, 이에 의해 본 발명의 범위가 제한되는 것이 아닌 점은 명백할 것이다. 따라서, 본 발명의 실질적인 범위는 첨부된 청구항들과 그것들의 등가물에 의하여 정의된다고 할 것이다.
<110> Genofocus, Inc.
<120> Method for Preparing Soluble Organophosphorus Hydrolase Using
Fusion Partner and Chaperon
<130> P13-B141
<160> 22
<170> KopatentIn 2.0
<210> 1
<211> 337
<212> PRT
<213> Flavobacterium sp KCTC2480
<400> 1
Met Ser Ile Gly Thr Gly Asp Arg Ile Asn Thr Val Arg Gly Pro Ile
1 5 10 15
Thr Ile Ser Glu Ala Gly Phe Thr Leu Thr His Glu His Ile Cys Gly
20 25 30
Ser Ser Ala Gly Phe Leu Arg Ala Trp Pro Glu Phe Phe Gly Ser Arg
35 40 45
Lys Ala Leu Ala Glu Lys Ala Val Arg Gly Leu Arg Arg Ala Arg Ala
50 55 60
Ala Gly Val Arg Thr Ile Val Asp Val Ser Thr Phe Asp Ile Gly Arg
65 70 75 80
Asp Val Ser Leu Leu Ala Glu Val Ser Arg Ala Ala Asp Val His Ile
85 90 95
Val Ala Ala Thr Gly Leu Trp Phe Asp Pro Pro Leu Ser Met Arg Leu
100 105 110
Arg Ser Val Glu Glu Leu Thr Gln Phe Phe Leu Arg Glu Ile Gln Tyr
115 120 125
Gly Ile Glu Asp Thr Gly Ile Arg Ala Gly Ile Ile Lys Val Ala Thr
130 135 140
Thr Gly Lys Ala Ala Pro Phe Gln Glu Leu Val Leu Lys Ala Ala Ala
145 150 155 160
Arg Ala Ser Leu Ala Thr Gly Val Pro Val Thr Thr His Thr Ala Ala
165 170 175
Ser Gln Arg Asp Gly Glu Gln Gln Ala Ala Ile Phe Glu Ser Glu Gly
180 185 190
Leu Ser Pro Ser Arg Val Cys Ile Gly His Ser Asp Asp Thr Asp Asp
195 200 205
Leu Ser Tyr Leu Thr Ala Leu Ala Ala Arg Gly Tyr Leu Ile Gly Leu
210 215 220
Asp His Ile Pro His Ser Ala Ile Gly Leu Glu Asp Asn Ala Ser Ala
225 230 235 240
Ser Ala Leu Leu Gly Ile Arg Ser Trp Gln Thr Arg Ala Leu Leu Ile
245 250 255
Lys Ala Leu Ile Asp Gln Gly Tyr Met Lys Gln Ile Leu Val Ser Asn
260 265 270
Asp Trp Leu Phe Gly Phe Ser Ser Tyr Val Thr Asn Ile Met Asp Val
275 280 285
Met Asp Arg Val Asn Pro Asp Gly Met Ala Phe Ile Pro Leu Arg Val
290 295 300
Ile Pro Phe Leu Arg Glu Lys Gly Val Pro Gln Glu Thr Leu Ala Gly
305 310 315 320
Ile Thr Val Thr Asn Pro Ala Arg Phe Leu Ser Pro Thr Leu Arg Ala
325 330 335
Ser
<210> 2
<211> 432
<212> PRT
<213> Escherichia coli
<400> 2
Met Ser Lys Ile Val Lys Ile Ile Gly Arg Glu Ile Ile Asp Ser Arg
1 5 10 15
Gly Asn Pro Thr Val Glu Ala Glu Val His Leu Glu Gly Gly Phe Val
20 25 30
Gly Met Ala Ala Ala Pro Ser Gly Ala Ser Thr Gly Ser Arg Glu Ala
35 40 45
Leu Glu Leu Arg Asp Gly Asp Lys Ser Arg Phe Leu Gly Lys Gly Val
50 55 60
Thr Lys Ala Val Ala Ala Val Asn Gly Pro Ile Ala Gln Ala Leu Ile
65 70 75 80
Gly Lys Asp Ala Lys Asp Gln Ala Gly Ile Asp Lys Ile Met Ile Asp
85 90 95
Leu Asp Gly Thr Glu Asn Lys Ser Lys Phe Gly Ala Asn Ala Ile Leu
100 105 110
Ala Val Ser Leu Ala Asn Ala Lys Ala Ala Ala Ala Ala Lys Gly Met
115 120 125
Pro Leu Tyr Glu His Ile Ala Glu Leu Asn Gly Thr Pro Gly Lys Tyr
130 135 140
Ser Met Pro Val Pro Met Met Asn Ile Ile Asn Gly Gly Glu His Ala
145 150 155 160
Asp Asn Asn Val Asp Ile Gln Glu Phe Met Ile Gln Pro Val Gly Ala
165 170 175
Lys Thr Val Lys Glu Ala Ile Arg Met Gly Ser Glu Val Phe His His
180 185 190
Leu Ala Lys Val Leu Lys Ala Lys Gly Met Asn Thr Ala Val Gly Asp
195 200 205
Glu Gly Gly Tyr Ala Pro Asn Leu Gly Ser Asn Ala Glu Ala Leu Ala
210 215 220
Val Ile Ala Glu Ala Val Lys Ala Ala Gly Tyr Glu Leu Gly Lys Asp
225 230 235 240
Ile Thr Leu Ala Met Asp Cys Ala Ala Ser Glu Phe Tyr Lys Asp Gly
245 250 255
Lys Tyr Val Leu Ala Gly Glu Gly Asn Lys Ala Phe Thr Ser Glu Glu
260 265 270
Phe Thr His Phe Leu Glu Glu Leu Thr Lys Gln Tyr Pro Ile Val Ser
275 280 285
Ile Glu Asp Gly Leu Asp Glu Ser Asp Trp Asp Gly Phe Ala Tyr Gln
290 295 300
Thr Lys Val Leu Gly Asp Lys Ile Gln Leu Val Gly Asp Asp Leu Phe
305 310 315 320
Val Thr Asn Thr Arg Ile Leu Lys Glu Gly Ile Glu Lys Gly Ile Ala
325 330 335
Asn Ser Ile Leu Ile Lys Phe Asn Gln Ile Gly Ser Leu Thr Glu Thr
340 345 350
Leu Ala Ala Ile Lys Met Ala Lys Asp Ala Gly Tyr Thr Ala Val Ile
355 360 365
Ser His Arg Ser Gly Glu Thr Glu Asp Ala Thr Ile Ala Asp Leu Ala
370 375 380
Val Gly Thr Ala Ala Gly Gln Ile Lys Thr Gly Ser Met Ser Arg Ser
385 390 395 400
Asp Arg Val Ala Lys Tyr Asn Gln Leu Ile Arg Ile Glu Glu Ala Leu
405 410 415
Gly Glu Lys Ala Pro Tyr Asn Gly Arg Lys Glu Ile Lys Gly Gln Ala
420 425 430
<210> 3
<211> 283
<212> PRT
<213> Escherichia coli
<400> 3
Met Ala Glu Ile Thr Ala Ser Leu Val Lys Glu Leu Arg Glu Arg Thr
1 5 10 15
Gly Ala Gly Met Met Asp Cys Lys Lys Ala Leu Thr Glu Ala Asn Gly
20 25 30
Asp Ile Glu Leu Ala Ile Glu Asn Met Arg Lys Ser Gly Ala Ile Lys
35 40 45
Ala Ala Lys Lys Ala Gly Asn Val Ala Ala Asp Gly Val Ile Lys Thr
50 55 60
Lys Ile Asp Gly Asn Tyr Gly Ile Ile Leu Glu Val Asn Cys Gln Thr
65 70 75 80
Asp Phe Val Ala Lys Asp Ala Gly Phe Gln Ala Phe Ala Asp Lys Val
85 90 95
Leu Asp Ala Ala Val Ala Gly Lys Ile Thr Asp Val Glu Val Leu Lys
100 105 110
Ala Gln Phe Glu Glu Glu Arg Val Ala Leu Val Ala Lys Ile Gly Glu
115 120 125
Asn Ile Asn Ile Arg Arg Val Ala Ala Leu Glu Gly Asp Val Leu Gly
130 135 140
Ser Tyr Gln His Gly Ala Arg Ile Gly Val Leu Val Ala Ala Lys Gly
145 150 155 160
Ala Asp Glu Glu Leu Val Lys His Ile Ala Met His Val Ala Ala Ser
165 170 175
Lys Pro Glu Phe Ile Lys Pro Glu Asp Val Ser Ala Glu Val Val Glu
180 185 190
Lys Glu Tyr Gln Val Gln Leu Asp Ile Ala Met Gln Ser Gly Lys Pro
195 200 205
Lys Glu Ile Ala Glu Lys Met Val Glu Gly Arg Met Lys Lys Phe Thr
210 215 220
Gly Glu Val Ser Leu Thr Gly Gln Pro Phe Val Met Glu Pro Ser Lys
225 230 235 240
Thr Val Gly Gln Leu Leu Lys Glu His Asn Ala Glu Val Thr Gly Phe
245 250 255
Ile Arg Phe Glu Val Gly Glu Gly Ile Glu Lys Val Glu Thr Asp Phe
260 265 270
Ala Ala Glu Val Ala Ala Met Ser Lys Gln Ser
275 280
<210> 4
<211> 638
<212> PRT
<213> Escherichia coli
<400> 4
Met Gly Lys Ile Ile Gly Ile Asp Leu Gly Thr Thr Asn Ser Cys Val
1 5 10 15
Ala Ile Met Asp Gly Thr Thr Pro Arg Val Leu Glu Asn Ala Glu Gly
20 25 30
Asp Arg Thr Thr Pro Ser Ile Ile Ala Tyr Thr Gln Asp Gly Glu Thr
35 40 45
Leu Val Gly Gln Pro Ala Lys Arg Gln Ala Val Thr Asn Pro Gln Asn
50 55 60
Thr Leu Phe Ala Ile Lys Arg Leu Ile Gly Arg Arg Phe Gln Asp Glu
65 70 75 80
Glu Val Gln Arg Asp Val Ser Ile Met Pro Phe Lys Ile Ile Ala Ala
85 90 95
Asp Asn Gly Asp Ala Trp Val Glu Val Lys Gly Gln Lys Met Ala Pro
100 105 110
Pro Gln Ile Ser Ala Glu Val Leu Lys Lys Met Lys Lys Thr Ala Glu
115 120 125
Asp Tyr Leu Gly Glu Pro Val Thr Glu Ala Val Ile Thr Val Pro Ala
130 135 140
Tyr Phe Asn Asp Ala Gln Arg Gln Ala Thr Lys Asp Ala Gly Arg Ile
145 150 155 160
Ala Gly Leu Glu Val Lys Arg Ile Ile Asn Glu Pro Thr Ala Ala Ala
165 170 175
Leu Ala Tyr Gly Leu Asp Lys Gly Thr Gly Asn Arg Thr Ile Ala Val
180 185 190
Tyr Asp Leu Gly Gly Gly Thr Phe Asp Ile Ser Ile Ile Glu Ile Asp
195 200 205
Glu Val Asp Gly Glu Lys Thr Phe Glu Val Leu Ala Thr Asn Gly Asp
210 215 220
Thr His Leu Gly Gly Glu Asp Phe Asp Ser Arg Leu Ile Asn Tyr Leu
225 230 235 240
Val Glu Glu Phe Lys Lys Asp Gln Gly Ile Asp Leu Arg Asn Asp Pro
245 250 255
Leu Ala Met Gln Arg Leu Lys Glu Ala Ala Glu Lys Ala Lys Ile Glu
260 265 270
Leu Ser Ser Ala Gln Gln Thr Asp Val Asn Leu Pro Tyr Ile Thr Ala
275 280 285
Asp Ala Thr Gly Pro Lys His Met Asn Ile Lys Val Thr Arg Ala Lys
290 295 300
Leu Glu Ser Leu Val Glu Asp Leu Val Asn Arg Ser Ile Glu Pro Leu
305 310 315 320
Lys Val Ala Leu Gln Asp Ala Gly Leu Ser Val Ser Asp Ile Asp Asp
325 330 335
Val Ile Leu Val Gly Gly Gln Thr Arg Met Pro Met Val Gln Lys Lys
340 345 350
Val Ala Glu Phe Phe Gly Lys Glu Pro Arg Lys Asp Val Asn Pro Asp
355 360 365
Glu Ala Val Ala Ile Gly Ala Ala Val Gln Gly Gly Val Leu Thr Gly
370 375 380
Asp Val Lys Asp Val Leu Leu Leu Asp Val Thr Pro Leu Ser Leu Gly
385 390 395 400
Ile Glu Thr Met Gly Gly Val Met Thr Thr Leu Ile Ala Lys Asn Thr
405 410 415
Thr Ile Pro Thr Lys His Ser Gln Val Phe Ser Thr Ala Glu Asp Asn
420 425 430
Gln Ser Ala Val Thr Ile His Val Leu Gln Gly Glu Arg Lys Arg Ala
435 440 445
Ala Asp Asn Lys Ser Leu Gly Gln Phe Asn Leu Asp Gly Ile Asn Pro
450 455 460
Ala Pro Arg Gly Met Pro Gln Ile Glu Val Thr Phe Asp Ile Asp Ala
465 470 475 480
Asp Gly Ile Leu His Val Ser Ala Lys Asp Lys Asn Ser Gly Lys Glu
485 490 495
Gln Lys Ile Thr Ile Lys Ala Ser Ser Gly Leu Asn Glu Asp Glu Ile
500 505 510
Gln Lys Met Val Arg Asp Ala Glu Ala Asn Ala Glu Ala Asp Arg Lys
515 520 525
Phe Glu Glu Leu Val Gln Thr Arg Asn Gln Gly Asp His Leu Leu His
530 535 540
Ser Thr Arg Lys Gln Val Glu Glu Ala Gly Asp Lys Leu Pro Ala Asp
545 550 555 560
Asp Lys Thr Ala Ile Glu Ser Ala Leu Thr Ala Leu Glu Thr Ala Leu
565 570 575
Lys Gly Glu Asp Lys Ala Ala Ile Glu Ala Lys Met Gln Glu Leu Ala
580 585 590
Gln Val Ser Gln Lys Leu Met Glu Ile Ala Gln Gln Gln His Ala Gln
595 600 605
Gln Gln Thr Ala Gly Ala Asp Ala Ser Ala Asn Asn Ala Lys Asp Asp
610 615 620
Asp Val Val Asp Ala Glu Phe Glu Glu Val Lys Asp Lys Lys
625 630 635
<210> 5
<211> 389
<212> PRT
<213> Artificial Sequence
<220>
<223> pMAL
<400> 5
Met Lys Ile Glu Glu Gly Lys Leu Val Ile Trp Ile Asn Gly Asp Lys
1 5 10 15
Gly Tyr Asn Gly Leu Ala Glu Val Gly Lys Lys Phe Glu Lys Asp Thr
20 25 30
Gly Ile Lys Val Thr Val Glu His Pro Asp Lys Leu Glu Glu Lys Phe
35 40 45
Pro Gln Val Ala Ala Thr Gly Asp Gly Pro Asp Ile Ile Phe Trp Ala
50 55 60
His Asp Arg Phe Gly Gly Tyr Ala Gln Ser Gly Leu Leu Ala Glu Ile
65 70 75 80
Thr Pro Asp Lys Ala Phe Gln Asp Lys Leu Tyr Pro Phe Thr Trp Asp
85 90 95
Ala Val Arg Tyr Asn Gly Lys Leu Ile Ala Tyr Pro Ile Ala Val Glu
100 105 110
Ala Leu Ser Leu Ile Tyr Asn Lys Asp Leu Leu Pro Asn Pro Pro Lys
115 120 125
Thr Trp Glu Glu Ile Pro Ala Leu Asp Lys Glu Leu Lys Ala Lys Gly
130 135 140
Lys Ser Ala Leu Met Phe Asn Leu Gln Glu Pro Tyr Phe Thr Trp Pro
145 150 155 160
Leu Ile Ala Ala Asp Gly Gly Tyr Ala Phe Lys Tyr Glu Asn Gly Lys
165 170 175
Tyr Asp Ile Lys Asp Val Gly Val Asp Asn Ala Gly Ala Lys Ala Gly
180 185 190
Leu Thr Phe Leu Val Asp Leu Ile Lys Asn Lys His Met Asn Ala Asp
195 200 205
Thr Asp Tyr Ser Ile Ala Glu Ala Ala Phe Asn Lys Gly Glu Thr Ala
210 215 220
Met Thr Ile Asn Gly Pro Trp Ala Trp Ser Asn Ile Asp Thr Ser Lys
225 230 235 240
Val Asn Tyr Gly Val Thr Val Leu Pro Thr Phe Lys Gly Gln Pro Ser
245 250 255
Lys Pro Phe Val Gly Val Leu Ser Ala Gly Ile Asn Ala Ala Ser Pro
260 265 270
Asn Lys Glu Leu Ala Lys Glu Phe Leu Glu Asn Tyr Leu Leu Thr Asp
275 280 285
Glu Gly Leu Glu Ala Val Asn Lys Asp Lys Pro Leu Gly Ala Val Ala
290 295 300
Leu Lys Ser Tyr Glu Glu Glu Leu Ala Lys Asp Pro Arg Ile Ala Ala
305 310 315 320
Thr Met Glu Asn Ala Gln Lys Gly Glu Ile Met Pro Asn Ile Pro Gln
325 330 335
Met Ser Ala Phe Trp Tyr Ala Val Arg Thr Ala Val Ile Asn Ala Ala
340 345 350
Ser Gly Arg Gln Thr Val Asp Glu Ala Leu Lys Asp Ala Gln Thr Asn
355 360 365
Ser Ser Ser Asn Asn Asn Asn Asn Asn Asn Asn Asn Asn Leu Gly Ile
370 375 380
Glu Gly Arg Ile Ser
385
<210> 6
<211> 97
<212> PRT
<213> Artificial Sequence
<220>
<223> pGro7
<400> 6
Met Asn Ile Arg Pro Leu His Asp Arg Val Ile Val Lys Arg Lys Glu
1 5 10 15
Val Glu Thr Lys Ser Ala Gly Gly Ile Val Leu Thr Gly Ser Ala Ala
20 25 30
Ala Lys Ser Thr Arg Gly Glu Val Leu Ala Val Gly Asn Gly Arg Ile
35 40 45
Leu Glu Asn Gly Glu Val Lys Pro Leu Asp Val Lys Val Gly Asp Ile
50 55 60
Val Ile Phe Asn Asp Gly Tyr Gly Val Lys Ser Glu Lys Ile Asp Asn
65 70 75 80
Glu Glu Val Leu Ile Met Ser Glu Ser Asp Ile Leu Ala Ile Val Glu
85 90 95
Ala
<210> 7
<211> 548
<212> PRT
<213> Artificial Sequence
<220>
<223> pGro7
<400> 7
Met Ala Ala Lys Asp Val Lys Phe Gly Asn Asp Ala Arg Val Lys Met
1 5 10 15
Leu Arg Gly Val Asn Val Leu Ala Asp Ala Val Lys Val Thr Leu Gly
20 25 30
Pro Lys Gly Arg Asn Val Val Leu Asp Lys Ser Phe Gly Ala Pro Thr
35 40 45
Ile Thr Lys Asp Gly Val Ser Val Ala Arg Glu Ile Glu Leu Glu Asp
50 55 60
Lys Phe Glu Asn Met Gly Ala Gln Met Val Lys Glu Val Ala Ser Lys
65 70 75 80
Ala Asn Asp Ala Ala Gly Asp Gly Thr Thr Thr Ala Thr Val Leu Ala
85 90 95
Gln Ala Ile Ile Thr Glu Gly Leu Lys Ala Val Ala Ala Gly Met Asn
100 105 110
Pro Met Asp Leu Lys Arg Gly Ile Asp Lys Ala Val Thr Ala Ala Val
115 120 125
Glu Glu Leu Lys Ala Leu Ser Val Pro Cys Ser Asp Ser Lys Ala Ile
130 135 140
Ala Gln Val Gly Thr Ile Ser Ala Asn Ser Asp Glu Thr Val Gly Lys
145 150 155 160
Leu Ile Ala Glu Ala Met Asp Lys Val Gly Lys Glu Gly Val Ile Thr
165 170 175
Val Glu Asp Gly Thr Gly Leu Gln Asp Glu Leu Asp Val Val Glu Gly
180 185 190
Met Gln Phe Asp Arg Gly Tyr Leu Ser Pro Tyr Phe Ile Asn Lys Pro
195 200 205
Glu Thr Gly Ala Val Glu Leu Glu Ser Pro Phe Ile Leu Leu Ala Asp
210 215 220
Lys Lys Ile Ser Asn Ile Arg Glu Met Leu Pro Val Leu Glu Ala Val
225 230 235 240
Ala Lys Ala Gly Lys Pro Leu Leu Ile Ile Ala Glu Asp Val Glu Gly
245 250 255
Glu Ala Leu Ala Thr Leu Val Val Asn Thr Met Arg Gly Ile Val Lys
260 265 270
Val Ala Ala Val Lys Ala Pro Gly Phe Gly Asp Arg Arg Lys Ala Met
275 280 285
Leu Gln Asp Ile Ala Thr Leu Thr Gly Gly Thr Val Ile Ser Glu Glu
290 295 300
Ile Gly Met Glu Leu Glu Lys Ala Thr Leu Glu Asp Leu Gly Gln Ala
305 310 315 320
Lys Arg Val Val Ile Asn Lys Asp Thr Thr Thr Ile Ile Asp Gly Val
325 330 335
Gly Glu Glu Ala Ala Ile Gln Gly Arg Val Ala Gln Ile Arg Gln Gln
340 345 350
Ile Glu Glu Ala Thr Ser Asp Tyr Asp Arg Glu Lys Leu Gln Glu Arg
355 360 365
Val Ala Lys Leu Ala Gly Gly Val Ala Val Ile Lys Val Gly Ala Ala
370 375 380
Thr Glu Val Glu Met Lys Glu Lys Lys Ala Arg Val Glu Asp Ala Leu
385 390 395 400
His Ala Thr Arg Ala Ala Val Glu Glu Gly Val Val Ala Gly Gly Gly
405 410 415
Val Ala Leu Ile Arg Val Ala Ser Lys Leu Ala Asp Leu Arg Gly Gln
420 425 430
Asn Glu Asp Gln Asn Val Gly Ile Lys Val Ala Leu Arg Ala Met Glu
435 440 445
Ala Pro Leu Arg Gln Ile Val Leu Asn Cys Gly Glu Glu Pro Ser Val
450 455 460
Val Ala Asn Thr Val Lys Gly Gly Asp Gly Asn Tyr Gly Tyr Asn Ala
465 470 475 480
Ala Thr Glu Glu Tyr Gly Asn Met Ile Asp Met Gly Ile Leu Asp Pro
485 490 495
Thr Lys Val Thr Arg Ser Ala Leu Gln Tyr Ala Ala Ser Val Ala Gly
500 505 510
Leu Met Ile Thr Thr Glu Cys Met Val Thr Asp Leu Pro Lys Asn Asp
515 520 525
Ala Ala Asp Leu Gly Ala Ala Gly Gly Met Gly Gly Met Gly Gly Met
530 535 540
Gly Gly Met Met
545
<210> 8
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 8
aaaaggatcc atgctgaaac cagaaatgat 30
<210> 9
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 9
aaaagaattc gttttgtgtg tcgagggtag 30
<210> 10
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 10
aaaaggatcc atgaatattc gtccattgca 30
<210> 11
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 11
aaaagaattc cgcttcaaca attgccagaa 30
<210> 12
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 12
aaaaggatcc atgaaatcca gaaaatggta 30
<210> 13
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 13
aaaagaattc ttttttgtct ttgacttctt 30
<210> 14
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 14
aaaaggatcc atgactgttc aaacaagtaa 30
<210> 15
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 15
aaaaggtacc acccgcgtaa gctgccagca 30
<210> 16
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 16
aaaaggatcc atggctgaaa ttaccgcatc 30
<210> 17
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 17
aaaaggtacc agactgcttg gacatcgcag 30
<210> 18
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 18
aaaaggatcc atgtccaaaa tcgtaaaaat 30
<210> 19
<211> 29
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 19
aaaaggtacc tgcctggcct ttgatctct 29
<210> 20
<211> 33
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 20
aaaagaattc atgtcgatcg gcacaggcga tcg 33
<210> 21
<211> 30
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 21
aaaaaagctt tcatgacgcc cgcaaggtcg 30
<210> 22
<211> 33
<212> DNA
<213> Artificial Sequence
<220>
<223> primer
<400> 22
aaaaggtacc atgtcgatcg gcacaggcga tcg 33
Claims (8)
- 다음 단계를 포함하는 수용성 유기인화합물 분해효소의 제조방법:
(a) 수용성 융합파트너 MBP(maltose binding Protein)를 코딩하는 유전자와 서열번호 1의 아미노산 서열을 가지는 유기인 화합물 분해효소를 코딩하는 유전자가 융합단백질로 발현되도록 삽입된 재조합 벡터 및 GroES/GroEL 샤페론을 코딩하는 유전자를 함유하는 재조합 벡터로 형질전환된 미생물을 배양하여 수용성 융합파트너와 유기인 화합물 분해효소의 융합단백질을 생성하는 단계; 및
(b) 상기 생성된 수용성 융합파트너와 유기인 화합물 분해효소의 융합단백질을 수득하는 단계.
- 삭제
- 삭제
- 제1항에 있어서, 상기 MBP(maltose binding Protein)는 서열번호 5의 아미노산 서열을 가지는 것을 특징으로 하는 수용성 유기인화합물 분해효소의 제조방법.
- 제1항에 있어서, 재조합 벡터의 골격벡터는 pRSET, pMAL(c2X), pET28a(+)및 pACE로 구성된 군에서 선택되는 것을 특징으로 하는 수용성 유기인화합물 분해효소의 제조방법.
- 제1항에 있어서, GroES/GroEL은 각각 서열번호 6 및 서열번호 7의 아미노산 서열을 가지는 것을 특징으로 하는 수용성 유기인화합물 분해효소의 제조방법.
- 제1항에 있어서, 형질전환된 미생물은 대장균인 것을 특징을 하는 수용성 유기인화합물 분해효소의 제조방법.
- 삭제
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