• KSBB Journal
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• 제10권3호
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• pp.231-236
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• 1995

Saccharomyces sake Kyokai No.7을 이용한 고정화 균체 반응기에서 연속 알콜생산시에 발효배지 성분을 1/10배 ~3/10배 범위에서 희석하여 사용할 때 균체의 생산성과 고정화 beads의 물리적 안정성이 장기적으로 유지되었다. Egg albumin hydrolysate (0.5%)와 phosphatidylcholine(0.5%)을 첨가한 발효배지를 3/10배 희석하여 공급할 때 $1.1lhr^{-1}$ 희석 율에서 최대 알콜생산성인 $69 g/\ell$-hr 이 얻어졌으며, 이는 무첨가물의 2/1011H 희석 발효배지의 최대치인 $46 g/\ell$-hr 에 비하여 50% 증가한 것이다.

• 방사성폐기물학회지
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• 제10권1호
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• pp.21-26
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• 2012

소듐냉각 고속로 (SFR) 핵연료 피복관 후보재료로 고려되고 있는 중형 규모의 HT9 단조품 소재에 대한 금속조직학적 영향을 고찰하였다. 시험 재료는 유도가열법을 이용하여 1.1톤 규모의 잉곳으로 성형한 후, $1170^{\circ}C$에서 고온 단조 및 공랭을 통하여 160mm 직경 및 7000mm 길이를 갖는 단조품으로 가공하여 반경방향으로 미세조직의 변화를 관찰하였다. 시험 결과 시험 재료는 페라이트-마르텐사이트 조직을 보였으며 합금 조성에 의하여 2~3%의 델타 페라이트 (delta ferrite)를 가짐과 동시에 반경방향의 냉각속도 차이에 의하여 최대 15%의 변태 페라이트 (transformed ferrite)를 함유함이 관찰되었다. 냉각곡선의 모델링과 시간-온도-변태 (TTT) 선도를 이용한 민감도 분석을 통하여 단조품의 직경을 120mm로 줄였을 경우 중심부의 변태 페라이트 형성을 억제할 수 있음을 제시하였다.

• KSBB Journal
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• 제8권1호
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• pp.42-48
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• 1993

Continuous degradation of formaldehyde by using a rotating disc contactor was investigated in this study. Peudomonas putida H-5K was selected as a mutant using N-methyl N'-nitro N-nitrosoguandine (250$\mu\textrm{g}$/$m\ell$), which showed 1.5 times higher ability of formaldehyde degradation than that of the parent strain. Enzyme activity for formaldehyde degradation released form Peudomonas putida H-5K showed the highest level of 6.2mo1/min/mg protein in the 2% glucose mineral medium containing 0.02% formaldehyde. Degradation of formaldehyde from the first stage in rotating disc contactor was 95% and 5% from the 4th stage when the reactor was fed with 0.02% or 0.04% formaldehyde solution at a rate of 20$m\ell$ per hour. Continuous degradation of formaldehyde using rotating disc contactor was above 95%o in the medium containing 0.04% formalchyde, at the medium feed ratc of 20$m\ell$ per hour.

• Journal of Microbiology and Biotechnology
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• 제19권12호
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• pp.1603-1611
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• 2009

High-cell-density cultivation of yeast was investigated using the agricultural waste products corn steep liquor (CSL) and molasses. The Saccharomyces cerevisiae KV-25 cell mass was significantly dependent on the ratio between C and N sources. The concentrations of molasses and CSL in the culture medium were statistically optimized at 10.25% (v/v) and 16.87% (v/v), respectively, by response surface methodology (RSM). Batch culture in a 5-l stirred tank reactor using the optimized medium resulted in a cell mass production of 36.5 g/l. In the fed-batch culture, the feed phase was preceded by a batch phase using the optimized medium, and a very high dried-cell-mass yield of 187.63 g/l was successfully attained by feeding a mixture of 20% (v/v) molasses and 80% (v/v) CSL at a rate of 22 ml/h. In this system, the production of cell mass depended mainly on the agitation speed, the composition of the feed medium, and the glucose level in the medium, but only slightly on the aeration rate.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2002년도 생물공학의 동향 (X)
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• pp.121-125
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• 2002

Rhodococcus rhodochrous IGTSS (ATCC 5396S) can break organo sulfur compounds such as dibenzothiophene. Since the environment for biodesulfurization process is invariably hydrophobic, parameters in hydrophobic systems should be examined. For the model oil, hexadecane-containing 5.43mM dibenzothiophene, the volumetric desulfurization rate was decreased with the oil-to-aqueous phase ratio up to 50%. The rate declined sharply after 48h because the cell activity, which is refreshed by medium exchange, was lost. To supply the exhausted nutrients, medium exchange was performed. At 30% oil phase, most of DBT was removed by medium exchange on 48h, and the rate was 2.03mg $DBT_{removed}/L_{dispersion}-hr.$ At 50% oil phase, medium exchange on 60h was performed and the rate was 1.79mg $DBT_{removed}/L_{dispersion}-hr.$ The 300mL flask system was scaled up to a 5-L bioreactor system. On 60 h, a medium exchange was performed and the rate was 5.28mg $DBT_{removed}/L_{dispersion}-hr.$ and all of DBT was removed. It means that we can use the biodesulfurization process even 10 the high oil-to-water phase by some appropriate methods such as controlled feeding of key nutrients and the dilution or removal of some toxic metabolites by continuous reactor.

• 대한기계학회논문집B
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• 제38권3호
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• pp.271-277
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• 2014

원자로 노심 입구에 위치한 내부 구조물들은 형상 및 노심 입구까지의 상대적 거리에 따라 노심 입구 유량분포에 상당한 영향을 미칠 수 있다. 본 연구에서는 원자로 내부 구조물 형상 처리 방법이 축소 APR+ 유동분포 예측 정확도에 미치는 영향을 조사하기 위해 상용 전산유체역학 소프트웨어인 ANSYS CFX R.14를 사용하여 원자로 내부 구조물들의 실제 형상을 고려한 계산을 수행하였고 다공성 매질 가정을 적용한 계산 결과와 비교하였다. 결론적으로 노심 입구 상류에 위치한 원자로 내부 구조물의 실제 형상을 고려함으로써 노심 입구 유량 분포를 더 정확하게 예측할 수 있었다. 따라서 충분한 계산 자원이 확보된 조건인 경우라면 정확한 노심 입구 유량분포를 계산하기 위해 노심 입구 상류에 위치한 원자로 내부 구조물들(예: 하부지지구조물 바닥판 및 노내 계측기 노즐 지지판)의 실제 형상을 고려해서 계산하는 것이 필요하다.

• KSBB Journal
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• 제11권3호
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• pp.353-359
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• 1996

Thiobacillus ferrooxidans를 이용한 보다 효율적이고 현장에 직접 응용할 수 있는 우라늄 침출공정을 개발하기 위하여 배양조건의 확립과 교반 반응기 및 이중기포탑 반융기에서의 우라늄 침출에 대한 연구 를 수행하였다. 배지의 초기 $Fe^{2+}$ 농도는 원광석 40g/L에 대하여 16.2g/L를 이용하는 것이 적합하였으며, 원광석의 업자는 작을수록 우라늄 침출율이 증가하였다. 또한 원광석의 첨가량이 많을수록 우라늄의 침출속도는 증가하였으나 침출율은 약간씩 감소하였다. 교반 반 응기 빛 이중기포탑 반응기에서의 우라늄 침출에 대한 실험을 최적조건에서 수행한 결과 교반 반응기에 서는 진탕배양기에서와 통일하게 12일 배양시 39.3%의 침출율로 5.5mgjL의 우라늄을 얻었다. 반면 이중기포탑 반응기에서는 교반 반응기에 비하여 세 균수가 2.4배 증가하였으며, 우라늄의 침출율과 침출된 우라늄 농도도 각각 91.4%와 12.8mgjL으로 교반 반응기 보다 2.3배 증가하였다. 이러한 결과는 이중기포탑 반응기에서는 충분한 양의 산소와 이산 화탄소의 공급과 원광석의 혼합이 잘됨으로써 세균 의 활성이 크게 증가하여 우라늄 침출이 향상된 것으로 추정된다.

• Biotechnology and Bioprocess Engineering:BBE
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• 제9권5호
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• pp.345-351
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• 2004

We investigated the anaerobic ammonium oxidation (anammox) reaction in a lab-stale upflow anaerobic sludge blanket (UASB) reactor. Our aim was to detect and enrich the organisms responsible for the anammox reaction using a synthetic medium that contained low concentrations of substrates (ammonium and nitrite). The reactor was inoculated with granular sludge collected from a full-scale anaerobic digestor used for treating brewery wastewater The experiment was performed during 260 days under conditions of constant ammonium concentration ($50\;mg\;NH_4^+-N/L$) and different nitrite concentrations ($50{\~}150\;mg\;NO_2-N/L$). After 200 days, anammox activity was observed in the system. The microorganisms involved in this anammox reaction were identified as Candidatus B. Anammoxidans and K. Stuttgartiensis using fluorescence in situ hybridization (FISH ) method.

• 상하수도학회지
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• 제10권4호
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• pp.119-126
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• 1996

Influence factors and efficiency characteristics for treatment of wastewater containing phenol were studied with using Pseudomonas sp. B3. It took 130 hours to remove phenol, when only activated sludge of terminal disposal palnt of sewage was innoculated in batch culture, but it was required just 36 hours, when bacteria degrading phenol and activated sludge were simultaneously innoculated. If only phenol an carbon source was used, it necessary 36 hours for biodegradation of phenol, while glucose was added to medium, it took 73 hours. It was revealed as excellent effluent and SVI, when the F/M ratio, COD and phenol concentration were 53mg/l and 1.2mg/l, respectively, and optimum F/M ratio was revealed 0.31. The reactor were seriously shocked as reducing hydraulic retention time at constant phenol concentration more than increasing phenol concentration at constant hydraulic retention time, when volumetric loading rate was increased to $0.8kg\;phenol/m^3{\codt}d$ from $1.6kg\;phenol/m^3{\codt}d$. And also the effluent phenol concentration was 34mg/l after starting 12 hours of shocking and reactor was recovered as steady state after 65 hours of changing in the former test. Although the effluent phenol concentration was maximum value with 12mg/l after starting 20 hours of shocking and reactor was recovered as steady state after 54 hours of changing in the later test.

• Environmental Engineering Research
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• 제10권6호
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• pp.283-293
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• 2005

Characteristics of sulfur-based autotrophic denitrification in a semi-continuous type reactor and the kinetic parameters were studied. Enriched autotrophic denitrifying culture was used for the reactor operation. Biomass growth on sulfur particles and in the liquid medium was monitored using the DAPI staining method. From the result of ion concentration changes and the biomass growth, maximum specific growth rate, ${\mu}_{max}$, and the half velocity constant, $K_M$, were estimated as $0.61\;d^{-1}$ and 3.66 mg/L, respectively. Growth yield coefficient, Y values for electron acceptor and donor were found as 0.49 gVSS/g N and 0.16 gVSS/g S. The biomass showed specific denitrification rate, ranging 0.86-1.13 gN/g VSS-d. A half-order equation was found to best simulate the denitrification process in the packed bed reactor operated in the semi-continuous mode.