• 산업기술연구
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• 제21권A호
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• pp.337-341
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• 2001

This study was carried out to screen the effective polymeric additives preventing wall growth during mycelial submerged cultivation of Ganoderma. lucidum. Effects of additives on mycelial growth and exo-polysaccharide (EPS) production in flask culture and jar fermenter system under 3 different pH processes were investigated, and changes of mycelial morphology were also examined. From flask culture of G. lucidum with additives of different concentrations, 0.1%(w/v) polyacrylic acid was effective for EPS production. As the polyacrylic acid of 0.1%(w/v) was added in medium, wall growth of G. lucidum mycelium grown in jar fermenter system could be protected. The addition of 0.1%(w/v) polyacrylic acid to medium was also improved the mycelial growth and EPS production in the later of submerged culture G. lucidum and no changes of mycelial morphology were observed.

• 한국식품과학회지
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• 제42권1호
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• pp.82-89
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• 2010

노루궁뎅이버섯 균사체(Hericium erinaceum)의 심부발효물로부터 기능성소재를 얻기 위하여 flask 배양에서 적당한 기본 배지를 선정하였고, jar fermenter에서 선정된 mushroom complete medium(MCM)에 수삼추출물을 첨가하여 최적 발효조건을 검토하였다. 기본 액체배지 중 수삼추출물이 0.5% 첨가된 MCM에서 $25^{\circ}C$, pH 5.5의 조건으로 10일 경과 후 5.89 g/L의 가장 높은 균사체 건조균체량(mycelial dry weight, MDW)을 나타내었다. 발효물의 대량생산을 위한 50 L jar fermenter의 액체배양에서도 $25^{\circ}C$, pH 5.5와 교반속도 120 rpm과 0.4 vvm의 통기속도로 최적화 되었으며, 이러한 조건하에서 5일 배양으로 최대 MDW인 4.28 g/L을 얻을 수 있었다. 또한 MCM에 첨가되는 수삼추출물의 양을 jar fermenter에서 검토한 결과, 수삼추출물 5%가 첨가되는 군(HE-GE-5)의 최적 발효조건하에서 4.93 g/L의 최대 건조균체량을 나타내었다. 한편 수삼추출물이 첨가된 노루궁뎅이버섯 균사체의 발효물의 특성을 검토하기 위하여 심부발효물의 조다당획분을 조제한 후 구성분과 면역활성을 살펴본 결과, 최대 MDW를 나타낸 수삼추출물 5% 첨가 심부발효물의 조다당(HE-GE-CP-5)은 주로 중성당(63.2%)과 함께 상당량의 산성당(19.3%)과 소량의 단백질(8.8%)로 구성됨을 알 수 있었으며 마이토젠과 골수세포 증식활성이 균사체만의 심부발효물 조다당보다 증강되고 있음을 알 수 있었다.

• KSBB Journal
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• 제8권5호
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• pp.438-445
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• 1993

유기칠 폐기물을 보다 효율적으로 처리하고자, 상 분리 혐기발효와 Chiorella 배양에 의한 생우분의 4 단계-복합처리를 시도하였다. 3배 희석 생우분을 6 일간 산발효시킨 발효액을 4 일의 수리학적 체류시 간으로 1차 에탄발효조에 공급했을 때, 평균 977ml/l C비ture/day의 바이오가스가 생산되었고, 1차 발효 폐액을 역시 4일의 체류시간으로 2차 메탄발효조에 공급했을 때 평균 428ml/l culture/day의 바이오 가스가 생산되었다. 1차 메탄발효의 바이오가스 생 산성은 재래의 단일조식과 비교했을 때 31.4% 증가 되었다. 또한 산발효과정, 1차 및 2차 에탄발효과정 의 유기물 제거율은 각기 71.8%, 42.6% 그리고 2 24.0%였다. 한편, 2차 메탄발효폐액은 Chiarella s sp. PSH3에 의해 10일의 체류시간으로 반연속배양 처리한 결과, 평균 1.8g/l culture/day(2.8$\times$106 cells/ml)의 조체가 생산되었고, 이 과정의 유기물 제거율은 73%였다. 이상의 4단계 처리과정을 통하 여 초발원료인 3배 희석 생우분의 COD가 51, 300ppm에서 최종단계인 Chiarella의 처리에 의해 평균 85ppm으로 감소되어 총유기물 제거율이 99.8 %에 달하였다. 이들의 결과는 유기질 폐기물의 효 율적 처리와 더불어 바이오가스와 균체단백질을 생산하는 복합처리계의 구성이 가능함을 나타낸다.

• 한국환경과학회지
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• 제18권3호
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• pp.325-331
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• 2009

This study was aimed to behaviour of organics and nitrogen on the upflow anaerobic reactor when a acid fermenter is added. Up flow anaerobic reactor (UAR) reaction will result which operates, COD removal efficiencies of reactor with nitrate loading rate 0.11, 0.66g/L/d were over 77%, but one with 1.0g/L/d was 73.5%. Especially, on NLR 0.11g/L/d, COD removal was 77% and nitrate removal efficiency was 93% simultaneously. The other side upflow anaerobic reactor and acid fermenter (UAR+AF) reaction will result witch operates, COD removal efficiencies of reactor with nitrate loading rate 0.11, 0.66g/L/d were over 85%, but one with 1.0g/L/d was 80%. Especially, on NLR 0.11g/L/d, COD removal was 85% and nitrate removal efficiency was 98% simultaneously. Also, without in reaction condition increase of influent nitrate concentration resulted in the linear decrease of nitrate removal efficiency and nitrate removal efficiency at influent nitrate-nitrogen 800mg/L was 50%. Alkalinity was increased theoretically by denitrification at low nitrate-N concentration, however, it was not increased theoretically at high nitrate-No 40% nitrate-N of UAR was denitrified until 70% height of reactor and 90% nitrate-N of UAR+AF was denitrified until 30% height of reactor Upflow anaerobic reactor was to occur accumulate acid, which TVA/Alkalinity is 0.3$\sim$0.47. Increase of NLR resulted increase of effluent alkalinity and TVA production

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2001년도 추계학술발표대회
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• pp.390-393
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• 2001

The optimal temperature, pH and aeration rate for spore production by Bacillus polyfermenticus SCD in 500 ml shake flask and 5-1 jar fermenter were found to be $32^{\circ}C$, 7.0 and 1.0 vvm. respectively. When batch culture processes was performed under optimized culture conditions. viable cells were $3.3{\times}10^{10}$ CFU/ml and spore cells were $3.3{\times}10^{10}$ CFU/ml. Fed-batch culture processes were also examined with regard to higer maximum viable cell and spore production. The highe viable cells and spores were obtained in 5-1 jar fermenter at 72 h cultivation time by strategy in an intermediate feeding mode with 60% glucose solution 150 ml and 5% soybean flour solution 150 ml fed to the fermenter twice, and the productivity of spore cells was significantly increased. Finally. volumetric productivity of spore cells on fed-batch culture indicated $9.9{\times}10^8$ CFU/ml/h, which was approximately 2 times higher than batch culture. Thus, fed-batch culture show a promise as an industrial production method.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2001년도 추계학술발표대회
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• pp.317-318
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• 2001

• KSBB Journal
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• 제16권3호
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• pp.307-313
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• 2001

The effects of agitaion and aeration on mycelial growth, exo-polysaccharide (EPS) production, and substrate consumption upon the submerged cultivation of G. lucidum were investigated, and the batch kinetics of the EPS fermentation of G. lucidum were interpreted as function of agitation speed and aeration rate. In a 2.6 L jar fermenter system, the optimum agitation speed and aeration rate for EPS production were determined to be 400 rpm and 1.0 vvm, respectively. The maximum production of EPS obtained was 15 g/L. The logistic model for mycelial growth fitted the experimental data better than that determined by the Monod and the two-thirds power models. The Luedeking-Piret equation adequately modelled the kinetic data obtained for product and substrate.

• Journal of Microbiology and Biotechnology
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• 제8권6호
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• pp.575-580
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• 1998

Cellulase production by batch culture using the Trichoderma reesei Rut C30 strain with various concentrations of Solka Floc with 1 % wheat bran was studied in a 2.5 I fermenter. The cellulase activity increased with Solka Floc concentration up to 5%. When 5% Solka Floc and 1% wheat bran were contained in the medium, carboxymethyl cellulose (CMC) and filter paper (FP) activities were 232.4 U/$m\ell$ and 21.25 U/$m\ell$, respectively. The productivity was 143.6 FPU $1^{-l}h^{-1}$ and the yield was 425 FPU/g. The colonial morphology of T. reesei Rut C30 grown on Avicel agar plates and the changes in mycelial morphology of T. reesei Rut C30 with culture time are also presented.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
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• pp.360-363
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• 2000

The anaerobic bacterium P. productus was known to produce acetate from CO, $CO_2$ and $H_2$. In this research the production of acetate at high concentration from carbon monoxide was studied. In this research the effect of $CO_2$, $H_2$, and CODH co-factor on cell growth and acetate production was studied. Also the toxicity of acetate on cell growth was examined. Acetate formation in lab scale fermenter was tested and specific acetate production rate of $0.43\;g/L \;{\cdot}\;hr\;{\cdot}\;O.D.$ was obtained and the concentration of the acetate obtained in a fermenter higher than 40g/L.

• 한국미생물·생명공학회지
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• 제10권2호
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• pp.95-100
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• 1982

절간고구마원료주정폐액을 이용하여 단세포단백질을 생산함과 동시에 폐액의 BOD를 제거할 목적으로 우수효모를 선발하고, 선발된 효모의 배양조건을 검토한 후 3$\ell$ -jar fermenter에 의한 통기 배양을 한 결과 다음과 같은 결론을 얻었다. 폐액을 여과한 여액의 조성은 BOD$_{5}$ 15700ppm, COD 36800ppm, 환원당 3300ppm, 총질소 710ppm, 고형물51800ppm, 조회분390ppm이었다. 우수효모로 선발된 Torulopsis candida FRI YA-15를 $25^{\circ}C$에서 48시간 진탕배양하였을 때, 배양폐액에 대한 균체수율은 3.38g/$\ell$, BOD$_{5}$ 및 COD제거율은 각각 38.9%, 31.8%이었다. T. candida의 최적생육초기 pH는 4.0이었으며, 최적배양온도는 35$^{\circ}C$였다. 설정된 초기PH 및 온도하에서 3$\ell$-jar fermenter를 사용하여 통기량 2vvm, 교반속도 100rpm으로 배양하였을 때, 배양 28시간후에 최대로 생육하였으며, 그 때 배양액에 대한 균체수율은 3.2g/$\ell$였다. 건조균체의 조단백질함량은 47.98%였다.