• KSBB Journal
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• 제13권2호
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• pp.141-146
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• 1998

To remove the low concentration of methane biologically, a three phase fluidized bed bioreactor immobilized with Methylosinus trichosporium OB3b was used. Optimum pH, temperature and bed height for the operation were pH7.0, 30$^\circ C$ and 150cm, respectively. For the inlet methane concentration of 100-400ppm and flow rate of 2-4L/min, the removal efficiencies of the bioreactor using the activated carbon as a carrier were the range of 54-71%, whereas those using the biosand were the range of 45-56%. It was found that activated carbon was more efficient than the biosand for the removal of methane. When aeration tank was equipped with the bioreactor, the removal efficiency increased to 6-13% and maximum removal rate obtained in the experiment was 1184mg.CH$_4$/min.

• Journal of Microbiology and Biotechnology
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• 제13권2호
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• pp.301-304
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• 2003

In this study, hydrogen sulfide ($H_2S$), ammonia ($NH_3$), and benzene, which represent the major odor from a natural leather process plant, were removed using a fluidized bed bioreactor and biofilter including Thiobacillus sp. IW and a MY microbial consortium. The critical removal rate was $12g m^{-3}h^{-1}\;for\;H_2S,\;11g m^{-3}h^{-1}\;for\;NH_3\;and\;28 g m^{-3}h^{-1}$ for benzene by the fluidized bed bioreactor, and $8.5g m^{-3}h^{-1}\;for\;H_2S\;7g m^{-3}h^{-1}\;for\;NH_3,\;and\;25 g m^{-3}h^{-1}$ for benzene in the biofilter. The average removal efficiency of $H_2S$, $NH_3$, and benzene by continuous operation for over 30 days with the fluidized bed bioreactor was $95{\pm}3\%,\;99{\pm}1\%,\;and\;98{\pm}5\%$, respectively, whereas that with the biofilter was $96{\pm}4\%,\;95{\pm}4\%,\;and\;97{\pm}3\%$, respectively. Therefore, the critical removal rate of $H_2S$, $NH_3$, and benzene was higher in the fluidized bed bioreactor, whereas the removal efficiency on the continuous operation was similar in both bioreactors.

• Applied Biological Chemistry
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• 제37권4호
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• pp.237-242
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• 1994

유동층 생물반응기에서의 anthocyanin 생산을 위하여 당근의 모상근배양을 검토하여 보았다. 이 생물반응기에서의 모상근의 성장은 2.5배 증가되었지만 anthocyanin 생산은 낮았다. 그러나 유동층 생물반응기에서의 anthocyanin 생산은 fungal elicitor의 처리에 의해 2.3배 향상되었다.

• Journal of Microbiology and Biotechnology
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• 제9권3호
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• pp.265-270
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• 1999

A three phase fluidized bed bioreactor immobilized with Thiobacillus sp. IW was tested to remove hydrogen sulfide and methylmercaptan with high loading rate. In a single gas treatment, the bioreactor removed 92- 98％ of hydrogen sulfide with loading rate of 15- 66 g/l/h and removed 87-98％ of methylmercaptan with loading rate of 14-60 gl/sup -1/h/sup -1/. In the mixed gas treatment, the removal efficiencies of hydrogen sulfide and methylmercaptan maintained at 89-99％ for various inlet loading rates and were not affected by the inlet loading ratio of both gases in low loading rates. When the inlet concentration of methylmercaptan increased 3.8 times and was maintained for 30 h to observe the response of the bioreactor to sudden environmental change, the removal efficiency of methylmercaptan was maintained at an average of 91％.

• KSBB Journal
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• 제17권1호
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• pp.26-32
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• 2002

세포의 다당류 xanthan을 생산하기 위하여 호기성 박테리아 X. campestris를 9 L 삼상유동층 생물반응기에서 연속적으로 배양하였다. 고점도 배양액에서 공기 기포를 분쇄하기 위하여 직경 8 mm 유리 유동입자를 사용하였다. 반응기 희석률을 증가시킴에 따라 세포 단위질량 당 xanthan 생성속도 및 생성된 xanthan의 분자량은 증가하였다. 산소공급제한이 발생하지 않을 경우 연속발효에서의 xanthan 비생성속도는 회분식 발효에서 제안된 상관식의 예측결과 보다 상당히 높은 값을 보였다.

• Journal of Microbiology and Biotechnology
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• 제17권2호
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• pp.320-324
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• 2007

The removal of hydrogen sulfide ($H_2S$) from aqueous media was investigated using Thiobacillus novellas cells immobilized on a $SiO_2$ carrier (biosand). The optimal growth conditions for the bacterial strain were $30^{\circ}C$ and initial pH of 7.0. The main product of hydrogen sulfide oxidation by T. novellus was identified as the sulfate ion. A removal efficiency of 98% was maintained in the three-phase fluidized-bed reactor, whereas the efficiency was reduced to 90% for the two-phase fluidized-bed reactor and 68% for the two-phase reactor without cells. The maximum gas removal capacity for the system was 254 g $H_2S/m^3/h$ when the inlet $H_2S$ loading was $300g/m^3/h(1,500ppm)$. Stable operation of the immobilized reactor was possible for 20 days with the inlet $H_2S$ concentration held to 1,100 ppm. The fluidized bed bioreactor appeared to be an effective means for controlling hydrogen sulfide emissions.

• KSBB Journal
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• 제19권3호
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• pp.206-209
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• 2004

벤젠의 제거에 효과적인 MY 혼합균주를 획득하였으며, 이중 우점종은 Rhodococcus ruber DSM 43338T로 밝혀졌다. MY 혼합균주가 함유된 유동층 생물반응기는 벤젠에 대한 임계 제거율 (critical removal rate)은 32 g/㎥ h로 나타났으며, 17일간의 연속가동에서도 안정적인 처리효율을 보여주어서, 벤젠의 제거에 뛰어난 성능을 보여주었다.

• 멤브레인
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• 제28권3호
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• pp.196-204
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• 2018

하수처리 혐기성 유동상 생물반응기(Anaerobic Fluidized Bed Bioreactor : AFBR)는 높은 표면적을 갖는 입상활성탄을 유동 메디아로 적용함으로써 생물막 형성 및 유지에 유리하며 이로 인해 우수한 유기물 제거 효율을 나타내나 처리된 유출수 내의 질소와 같은 영양염류의 잔존이 여전히 문제로 남아있다. 본 연구에서는 AFBR에 의해 처리된 유출수 내의 질소 배제를 위하여 정삼투막(FO membrane)을 유도용액의 종류와 농도에 따라 적용하였다. 실험결과 유출수의 총질소 배제 효율은 FO막에 적용하는 유도용액(draw solution : DS)의 종류 및 농도에 크게 의존하였다. 유도용액 농도가 증가함에 따라 FO막의 수투과량이 증가하였으며, 1 M의 NaCl을 유도용액으로 사용한 경우 총질소 배제 효율은 55%이었으나 1 M의 glucose를 유도용액을 사용한 경우 거의 완벽한 총질소 배제 효율을 나타내었다. AFBR 유출수를 FO막으로 24시간 동안 여과를 진행하였으나 파울링에 의한 수투과량의 감소는 관찰되지 않았다.

• 한국미생물·생명공학회지
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• 제17권6호
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• pp.611-618
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• 1989

Cephalosporium acremonium 균주로 미생물 고정화 증식입자를 제조하여 유동층 생물반응기에서 세파로스포린 C 생산에 대한 메치오닌의 영향에 대하여 연구하였다. 메치오닌은 세파로스포린 C 생합성에 매우 중요한 대사조절인자로 알려져 있는데, 본고에서는 초기 발효배지 내 메치오닌 농도의 영향과 이를 토대로 생물반응기에 메치오닌을 주입하였을 때 세파로스포린 C 생산에 미치는 메치오닌의 영향을 관찰하였다. 초기 배지 내에 존재하는 메치오닌에 의해 세파로스포린 C 생산성이 증가하였으며, 메치오닌의 최적양(0.3-0.5w/v％)이 존재하였다. 또한 메치오닌에 의해 탄소원의 소모속도가 증가됨이 관찰되었다. 배지내 메치오닌이 고갈될 때 세파로스포린 C 생산이 극대화되었으나 유동층 생물반응기에서 메치오닌을 부가적으로 첨가하였을 때 그 효과는 기대한 수준에 미치지 못했는데 이는 생체내 메치오닌의 축적과 관계가 있는 것으로 판단되었다. 또 고정화 증식입자를 사용하였을 때 세파로스포린 C 생산에 양호한 결과를 얻었는데 이 경우에도 적정량의 메치오닌 투여가 생산성에 중요한 인자임을 발견하였다. 따라서 유동층 반응기의 운전에 의해 세포로스포린 C 생산성을 향상시키기 위해서는 초기 운전단계에서 최적양의 메치오닌을 주입하는 것이 가장 중요하며 고정화 증식입자의 사용에 의해 공정생산성을 획기적으로 증대시킬 수 있다고 판단되었다.

• 한국환경보건학회지
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• 제19권2호
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• pp.23-33
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• 1993

The anaerobic digestion of organic synthetic wastewater in anaerobic fluidized bed bioreactor (AFBBR) and anaerobic fluidized packed bed bioreactor (AFPBBR) was studied. This study was conducted to evaluate efficiency and reliability of two reactor. Experiment was performed to find the effect of upflow rate with AFBBR and the height of packed bed with AFPBBR. As a result, this program obtained several conclusion. These are given as follows: As applied the upflow rate increased in AFBBR the produced volume of biogas increased, while the gas production and COD removal decreased at above 0.3 m$^3$/h. When a upflow rate is 0.4 m$^3$/h in AFBBR the volatile suspended solid (VSS) became significantly increased. At an organic loading rate from 0.1 to 0.4 of upflow rate in AFBBR, the methane yield was 1.5584 m$^3$CH$_4$/kgCOD removed, and the observed cell yield coefficient was 0.0933 gVSS/gCOD. In case of AFPBBR, the results showed also that 20 cm of height of packed bed was superior to other in the aspect ot biogas production, the content of methane and COD removal. At 20 cm of height, the profile of microorganisms was stable, while at 30 cm the VSS of effluent became higher than AFBBR. Though COD removal of AFPBBR increased with packed bed, COD removal deteriorate with over packing because the loss of pressure became higher in the reactor. At an organic loading rate from 20 to 40 cm of packed bed in-AFPBBR, the methane yield was 2.5649 m$^3$CH$_4$/kgCOD removed, and the observed cell yield coefficient was 0.0506 gVSS/gCOD. Based upon the results obtained, it is suggested that AFBBR and AFPBBR is the most effective conditions at 0.3 m3/h of upflow rate, the 20cm of packed bed, respectively. The rate constant are summarized as follow: