• 제목/요약/키워드: oxygen production rate

검색결과 402건 처리시간 0.031초

Cellulolytic Enzymes Production Cultivation Using Air Circulation Bioreactor

  • Seo, Jin-Ho;Song, Hyo-Jung;Kim, Seong-Jun
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2005년도 생물공학의 동향(XVII)
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    • pp.232-237
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    • 2005
  • The cellulloytic enzymes, such as FPase and amylase, production by Trichoderma inhamatum KSJ1 using 10L air circulation bioreactor were tried. Physical properties of the employed bioreactor, mixing time, $k_{L}$ a were examined in airflow conditions of enzyme production cultures. Mixing time of distilled water at 0.6, 1.2, 1.8 vvm were 25, 21, 9 sec, respectively, and mandel's medium using rice straw and pulp as carbon sources were 31, 25, 15 sec. Mixing time decreased when airflow rate increased. $k_L$ a of distilled water at 0.6, 1.2, 1.8 vvm were measured -22.52, -29.31, -39.62, respectively, and the mandel's medium were -47.8, -18.5, -21.4. The $k_L$ a values was increased linearly as the air-flow rates increased. However the values in mandel's medium showed different results, especially at 0.6 vvm. Amylase and FPase activity at the 1.2 vvm was 3.39U/mL, 0.72U/mL in 5 days cultivation. and the activities at 0.6 vvm were 2.01U/mL, 0.39U/mL, respectively. The enzyme productivity at 1.2 vvm was higher than at 0.6 vvm, indicating that high oxygen tension is requested for the efficient enzyme production culture of T. inhamatum KSJ1.

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Preliminary Study of Seed Production of the Micronesian Mud Crab Scylla serrata (Crustacea: Portunidae) in Korea

  • Yi, Soon-Kil;Lee, So-Gwang;Lee, Jeong-Mee
    • Ocean and Polar Research
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    • 제31권3호
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    • pp.257-264
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    • 2009
  • Seventeen females of the mud crab Scylla serrata, from the State of Kosrae, Micronesia, were transported to the Fisheries Resources Research Institute, Gyeongsangnam-do, in oxygen-filled plastic bags. After acclimatization to a $30^{\circ}C$ holding temperature, nine females were selected for seed production trials. Spawning was hastened using eyestalk ablations; however, this may not be required in commercialscale mud crab seed production. Primary spawning produced an average of 2.4 million hatched larvae, whereas secondary spawning produced 0.4 million. About 10 days elapsed between spawning and hatching and 30 days between hatching and crablet. Mass mortalities up to 90% were observed between stages zoea 1 and zoea 2 in every trial. The highest survival rate from zoea 1 to crablet was estimated at 0.25%. Most commercial shrimp hatcheries in Korea are equipped with almost all necessary facilities and could be converted easily to mud crab hatcheries, able to run three to four times per year using hatchery technologies developed for blue crabs and Chinese mitten crabs.

동해 울릉분지 퇴적물에서 유기탄소 순환 (Organic Carbon Cycling in Ulleung Basin Sediments, East Sea)

  • 이태희;김동선;김부근;최동림
    • Ocean and Polar Research
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    • 제32권2호
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    • pp.145-156
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    • 2010
  • This study investigated organic carbon fluxes in Ulleung Basin sediments, East Sea based on a chamber experiment and geochemical analyses. At depths greater than 2,000 m, Ulleung Basin sediments have high organic carbon contents (over 2.0%). Apparent sedimentation rates (ASR) calculated from excess $^{210}Pb$ activity distribution, varied from 0.036 to $0.047\;cm\;yr^{-1}$. The mass accumulation rates (MAR) calculated from porosity, grain density (GD), and ASR, ranged from 131 to $184\;g\;m^{-2}\;yr^{-1}$. These results were in agreement with sediment trap results obtained at a water depth of 2100 m. Input fluxes of organic carbon varied from 7.89 to $11.08\;gC\;m^{-2}\;yr^{-1}$ at the basin sediments, with an average of $9.56\;gC\;m^{-2}\;yr^{-1}$. Below a sediment depth of 15cm, burial fluxes of organic carbon ranged from 2.02 to $3.10\;gC\;m^{-2}\;yr^{-1}$. Within the basin sediments, regenerated fluxes of organic carbon estimated with oxygen consumption rate, varied from 6.22 to $6.90\;gC\;m^{-2}\;yr^{-1}$. However, the regenerated fluxes of organic carbon calculated by subtracting burial flux from input flux, varied from 5.87 to $7.98\;gC\;m^{-2}\;yr^{-1}$. Respectively, the proportions of the input flux, regenerated flux, and burial flux to the primary production ($233.6\;gC\;m^{-2}\;yr^{-1}$) in the Ulleung Basin were about 4.1%, 3.0%, and 1.1%. These proportions were extraordinarily higher than the average of world open ocean. Based upon these results, the Ulleung Basin might play an integral role in the deposition and removal of organic carbon.

다시마(Saccharina japonica)의 생장에 따른 영양염 및 CO2 흡수율과 광합성 특성 변화 (Variations in Nutrients & CO2 Uptake Rates and Photosynthetic Characteristics of Saccharina japonica from the South Coast of Korea)

  • 황재란;심정희;김정배;김숙양;이용화
    • 한국해양학회지:바다
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    • 제16권4호
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    • pp.196-205
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    • 2011
  • 국내 해조류 양식종인 다시마(Saccharina japonica (Laminaria japonica Areschoug))의 영양염 및 무기탄소 흡수율과 광합성 특성을 살펴보기 위해, 부산시 기장군 일광해역 양식장에서 2011년 l월부터 5월동안 시료를 채집하여 실내 배양하였다. 배양 시료의 엽장과 엽폭 범위는 각각 46~288 cm, 4.8~22.0 cm였으며, 이들의 용존산소 평균 생산율은 $6.9{\pm}5.8{\mu}mol\;g^{-1}$ fresh weight(FW) $h^{-1}$, 질산염과 인산염 흡수율은 각각 $175.6{\pm}161.1\;nmol\;g^{-1}\;FW\;h^{-1}$, $12.7{\pm}10.1\;nmol\;g^{-1}\;FW\;h^{-1}$ 그리고 용존무기탄소 흡수율은 $8.9{\pm}7.9{\mu}mol\;g^{-1}\;FW\;h^{-1}$이었다. 다시마 엽장에 따른 이들 성분의 생산/흡수율은 로그함수 관계를 보여, 엽장 100~150 cm 이상부터는 다시마의 광합성 및 생장율이 다소 둔화되는 것으로 나타났다. 용존 산소 생산율과 질산염, 인산염, $TCO_2$ 흡수율은 각각 음의 선형관계를 보였으며, 특히 용존산소 생산율과 $TCO_2$ 흡수율은 높은 상관관계 ($r^2$=0.94)를 나타내어 서로에 대한 간접 지표가 될 수 있음을 의미한다. 다시마의 최대양지수율($F_v/F_m$)과 용존산소 및 무기탄소 생산/흡수율사이에 선형관계가 나타났으며, 양자수율이 높을수록 활발한 광합성작용으로 용존산소 생산이 활발함을 증명하였다. 광합성 형광특성 중 최대상대전자전달률은 비교적 엽체가 생장할수록 증가하였으며, 엽체의 부착부에 비해 상부 말단으로 갈수록 증가하였다. 이는 다시마가 생장할수록 광합성활성 조직 비(단위 면적당 습중량)가 증가하여 나타난 결과로 사료된다. 기장해역에서 다시마에 의한 연간 무기탄소 흡수량은 $1.0\sim1.7{\times}10^3C$ ton으로 추정되며, 이는 부산시 이산화탄소 배출량의 0.02~0.03%에 해당한다. 따라서 해조류에 의한 연안의 탄소 및 물질순환과 지구시스템에서의 역할을 파악하기 위해 추가적인 연구가 필요할 것으로 생각된다.

Production of ColE1 Type Plasmid by Escherichia coli $DH5\alpha$ Cultured Under Nonselective Conditions

  • PASSARINHA L. A.;DIOGO M. M.;QUEIROZ J. A.;MONTEIRO G. A.;FONSECA L. P.;PRAZERES D. M. F.
    • Journal of Microbiology and Biotechnology
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    • 제16권1호
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    • pp.20-24
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    • 2006
  • Plasmid DNA (pDNA) is a product of interest for many biopharmaceutical companies and research laboratories, because of increase in the number of gene therapy protocols that use nonviral vectors. This work was undertaken to study the effect of antibiotic and dissolved oxygen concentration (DOC) on the production of a ColE 1-type plasmid (pVAX1-LacZ) hosted in Escherichia coli $DH5\alpha$ and cultured in a batch fermentor with 0.751 of Terrific Broth. A decrease in the DOC from $60\%\;to\;5\%$ was shown to increase the specific pDNA concentration approximately 1.5-fold, due to the downregulation of growth. Additionally, this increase in the pDNA concentration led to a 2.2-fold increase in the purity of cell lysates obtained after cell lysis. However, the use of higher DOC led to 2.8-fold higher volumetric productivity as a consequence of a faster growth rate, reducing the fermentation time from 24 to 8 h. Interestingly, the specific pDNA concentration, and pDNA productivity and purity were always higher $(10-15\%)$ in the absence of antibiotic. Overall, the data indicate that nonselective conditions can be used without compromising yield, productivity, and purity of pDNA.

PR 제거공정 적용을 위한 오존 수 생성기술 연구 (A Study on the Ozonized Water Production technology for the PR Strip Process)

  • 손영수;채상훈
    • 대한전자공학회논문지SD
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    • 제41권12호
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    • pp.13-19
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    • 2004
  • 반도체 또는 평판디스플레이 제조에 있어 노광공정 후의 PR(photo-resist) 제거 공정으로서 기존의 황산기반 용액을 대체하는 고농도 오존 수 생성 기술에 대한 연구를 수행하였다. 세라믹 연면방전구조의 오존발생장치를 개발하여, 0.5[ℓ/min]의 산소 유량에서 최대 12[wt%]이상의 오존가스 농도를 얻었으며, 이를 고농도로 물과 혼합하기 위한 고효율 오존접촉장치를 개발하였다. 오존 수 생성 실험 결과, 오존가스 10[wt%]에서 80[ppm]이상의 오존 수 농도를 달성하였으며, 70[ppm]의 오존 수에서 PR 제거율 147[nm/min]의 양호한 결과를 얻었다.

혐기성 소화 효율 향상을 위한 초음파 주파수의 순차적 적용에 대한 연구 (A Study on Sequential-Frequency Sonication for Improving Anaerobic Digestion)

  • 황규대;박성한
    • 상하수도학회지
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    • 제25권6호
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    • pp.893-906
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    • 2011
  • The effect of ultrasound pretreatment on sludge degragability was investigated at different condotions: ultrasonic frequency(28, 40, 50kHz), intensity(10, 25, 50W), sonication time(10, 20, 30, 60min). Total suspended solid(TSS) and soluble chemical oxygen demand(SCOD) concentration were measured for the evaluation of pretreatment efficiency. The pretreated sludge was used as the feedstock for anaerobic digestion process. Biogas production and volatile suspended solid(VSS) removal were determined for evaluating the process performance. 1. TSS concentration of the sludge decreased at a constant rate as sonication operation was applied. The degradation rate of TSS increased when ultrasound frequency was decreased from 50kHz to 28kHz and intensity was increased from 10W to 50W. Efficiency of TSS degradation per input energy increased as ultrasonic frequency and intensity were decreased. At the frequency of 28 and 40kHz, SCOD concentration rapidly increased during the initial 30min of sonication time, and then it gradually increased. At 50kHz, SCOD concentration constantly increased for 60min of the sonication time. The SCOD production rate increased with increasing intensity under all ultrasound frequencies. 2. The optimum condition of ultrasound treatment was 28kHz, 50W and 60min for maximizing the biogas production, methane fraction, VSS removal. The highest values in biogas production, methane fraction in biogas, VSS removal were 370ml, 70%, 2.45g, respectively. Methane production rate per input energy increased at ultrasonic frequency and intensity decreased. 3. When raw sludge was pretreated at the condition of ultrasonic frequency of 28 and 40kHz in series, sequential-frequency sonication, intensity of 50W and 60min, biogas production, methane fraction, VSS removal were about the same that of 28kHz single-frequency sonication. When sequential-frequency sonication of 28 and 50kHz was applied in series, biogas production, methane fraction, VSS removal were 356 ~ 423ml, 69 ~ 71%, 2.41 ~ 2.78g, respectively. The pretreatment efficiency of 28-50kHz sequential-frequency sonication which sonication time of 28kHz and 50kHz was 40min and 20min was higher than that of 28kHz single-frequency sonication.

재조합 단백질 생산을 위한 곤충세포의 배양 (Insect Cell Cultures for Recombinant Protein Production)

  • 박영민;정용주양재명정인식
    • KSBB Journal
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    • 제4권3호
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    • pp.266-270
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    • 1989
  • 실험실 규모의 배양기에서 곤충세포의 배양을 수행하였다. 회분식 배양에서의 곤충 세포의 성장은 serum의 농도, 다른 영양소, 초기 정종 농도, 기계적인 교반파 같은 변수에 의해 영향을 받는 것으로 나타났다. Lactate와 ammonium은 회분식 배양에서의 말기에 관찰되는 농도에서는 세포의 성장을 저해하는 원인은 아닌것 같았다. 또한. redox potential은 공충세포의 배양 용존산소를 측정할 수 있는 좋은 index 임을 알 수 있었다. 아울러 유전공학적으로 재조합된 baculovirus를 곤충세포에 감염시켜 재조합 단백질의 생산을 시도하였으며 dilution rate 가 $0.006\;hr^{-1}$일때 반응기당 최대 2800 units 의 beta-galactosidase 가 생산되었다.

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이중실관 생물 반응기에서의 구연산 생산과 Scale-up (Citric Acid Production and Scale-up in Dual Hollow Fiber Bioreactor)

  • 장호남;지동진;심상준
    • 멤브레인
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    • 제2권2호
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    • pp.122-128
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    • 1992
  • 여러 크기의 이중실관 생물 반응기에서의 Aspergillus niger(KCTC 1232)를 이용한 구연산 생산 실험을 수행하였다. 초종 세포농도는 세포 성장구간 기준으로 300g/l에 달하였다. 공기와 산소의 공급 조건하에서의 단위 용적당의 생산성은 각각 0.63, 0.02g/l.h였고 이는 회분식 발효에 대해 10, 16배 증가한 결과이다. 공급배지의 초기 pH는 구연산의 생산에 중요한 요소이며 pH가 낮을수록 높은 구연산 생산수율을 얻을 수 있었다. Scale-up의 가능성을 알아보기 위해 반응기 unit와 배지의 공급속도를 변화시킨 결과 반응기 unit와 배지 공급속도의 증가는 기질의 높은 소비속도로 인해 생산성의 증가를 가져왔다.

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Inter-scale Observation and Process Optimization for Guanosine Fermentation

  • Chu, Ju;Zhang, Si-Liang;Zhuang, Ying-Ping
    • 한국미생물생명공학회:학술대회논문집
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    • 한국미생물생명공학회 2005년도 2005 Annual Meeting & International Symposium
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    • pp.233-244
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    • 2005
  • Guanosine fermentation process can be well predicted and analyzed by the proposed state equations describing the dynamic change of a bioreactor. Pyruvate and alanine were found to be characteristically accumulated along with the decline of the guanosine formation rate during the mid-late phase of the process. The enzymological study of the main pathways in glucose catabolism and the quantitative stoichiometric calculation of metabolic flux distribution revealed that it was entirely attributed to the shift of metabolic flux from hexose monophosphate (HMP) pathway to glycolysis pathway. The process optimization by focusing on the restore of the shift of metabolic flux was conducted and the overcoming the decrease of oxygen uptake rate (OUR) was taken as the relevant factor of the trans-scale operation. As a result, the production of guanosinewas increased from 17 g/L to over 34 g/I.

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