Abstract
For the mass production of DFAIII and for the development of techniques of separation and purification of it, the methods of production of DFAIII and its recovery was investigated by fermentation with the strain of Arthrobacter ureafaciens KCTC 3387 and by enzyme reaction. In the first method, DFAIII was produced by fermentation with the strain of Arthrobacter ureafaciens KCTC 3387 and recovered from culture supernatant with silica gel gy filtration, in the second method, it was produced by enzyme reaction and recoverd with the same method of the first, and in third method it was produced by fermentation and recovered by addition of ethanol to the culture supernatnat.Against 25g/L of initial concentration of inulin, 1.57, 4.40, 0.34 g/L of powder of DFAIII was recovered respectively and the rate of recovery was 6.3, 17.6 1.4% and the purity was estimated at 81, 97, 87% respectively. For the production of DFAIII and its recovery, enzyme reaction method was the highest in the rate of recovery and its purity. By fermentation method, DFAIII was produced with 50% fo initial concentration of substrate but th rate of recovery was lower than enzyme reaction method and purity was lowest among the three methods. Ethanol pricipitation method showed the lowest rate of recovery.
의 대량생산과 분리.정제 기술의 개발을 위해 Arthrobacter ureafaciens KCTC 3387 균주를 이용한 발효 및 분리정제된 효소반응을 통한 DFAIII의 생산과 회수에 대하여 조사하였다. 첫 번째 방법으로는 Arthrobacter ureafaciens 균주를 발효배양하여 DFAIII 양이 최고가 되는 시점에서 발효정지 시킨후 silica gel를 통해 gel filtration을 분리하였고, 두 번째 방법으로는 정제된 효소로 반응시킨 다음 silica gel을 통해 gel filtration을 하여 분리하였으며, 세 번째 방법으로는 발효배양상등액에 에탄올을 첨가하여 생산물을 침전시켜 DFAIII를 분리하였다. 25 g/L의 초기 inulin 농도로부터 각각 1.57, 4.40, 0.34 g/L 의 정제분말이 얻어져 각각 6.3, 17.6, 1.4%의 수율로 회수되었고, 81, 97, 87%의 순도를 각각 나타내었다. 효소반응을 통한 DFAIII 생산 및 회수가 가장 높은 수율과 순도로 회수되었으며, 발효배양을 통한 DFAIII의 생산은 초기기질농도 25 g/L의 50%에 해당하는 DFAIII가 생산되었으나 효소반응에 의한 생산보다는 낮은 수율로 회수되었고 순도는 세 가지 방법 중 가장 낮았으며, 에탄올 침전반응은 가장 낮은 수율을 나타내었다.
