• Fisheries and Aquatic Sciences
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• 제14권4호
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• pp.371-378
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• 2011

Juvenile red seabream (mean body weight 29.0 g) were reared in recirculating culture systems with three different biofilter media, sand (SF), polystyrene microbeads (PF), and Kaldnes beads (KF). The efficiencies of the three different biofilter media were also tested. The SF was fluidized, and the PF and KF were trickled. All treatments were duplicated. The volumetric removal rates of total ammonia nitrogen by SF, PF, and KF were 193.8, 183.9, and 142.6 g $m^{-3}day^{-1}$, respectively, and those of nitrite nitrogen ($NO_2$-N) were 113.4, 105.9, and 85.8 g $m^{-3}day^{-1}$, respectively. The TAN and $NO_2$-N removal rates of KF were lower than those of SF and PF (P < 0.05), but there was no significant difference in these rates between SF and PF (P > 0.05). Among the biofilters used, only KF showed total suspended solid (TSS) removal capacity. The TSS removal efficiencies of SF and PF were negative. The growth rates of fish in SF were significantly higher than those in KF but not higher than those in PF. There was no difference in growth rate between fish in PF and KF. The specific growth rate and feed conversion efficiency of red seabreams in KF were lower than those in SF and PF, but there were no significant differences between SF and PF. These results indicate that sand and polystyrene microbeads are recommended for red seabream culture in a recirculating system.

• Journal of Biosystems Engineering
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• 제28권5호
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• pp.457-464
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• 2003

The purpose of this study was to develop a pilot scale bio-filter system removing ammonia gas with microorganisms. The system consisted of chaff(filter medium), a blower, a temperature sensor, a moisture sensor, a solenoid valve, and a heating system. Temperature and moisture contents were controlled via a PC to provide the microorganisms with proper environment. The microorganisms used in this study were Bacillius. coagulans NLRI T-6 and Pseudononas. putida NLRI S-21 of bacilli. Performance tests were performed to evaluate gas removal rate during 20 days. The result was shown that the removal rate was high in early days and gradually dropped below 90% without injecting the microbes. However, it was shown that when injecting the microbes, the removal rate was almost 100% and pH value was maintained at between 7 and 9 during the whole twenty-day period.

• 한국축산시설환경학회지
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• 제13권3호
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• pp.195-200
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• 2007

무창 육성 비육돈사에 대한 악취 제어 효율 비교분석을 위하여 Biofilter 덕트에 의한 악취 제어 연구를 수행하였다. 본 실험은 서울대 부속목장 실험돈사에서 실시하였으며 실험결과는 다음과 같다. 1. 무창 육성비육돈사에서 여름철 최대 배기시 바이오필터 외부로 배출되는 공기속도는 볏짚(.0.77 m/s), ALC(0.56 m/s)으로 측정되었다. 2. 실험시작 5일 후 가스검지기(GV-100)에 의한 간이측정시 암모니아($NH_3$) 농도는 필터 통과 후 볏짚($2mg/{\ell}$), ALC(3ppm)로 측정되어 부자재 사이의 공극율이 높은 볏짚이 높게 나타났다. 부자재에 따른 필터외부에서의 먼지측정 결과 볏짚($93\;mg/m^3$), ALC($32\;mg/m^3$)으로 측정되어 볏짚은 볏짚 간의 넓은 공극에서 발생하는 먼지 및 돈사내부의 먼지가 혼합되어 필터 외부로 배출되어 돈사내부보다 높게 측정되었다. 3. 황화수소($H_{2}S$) 가스농도 변화는 돈사내부에서는 측정일 7일(6 ppm), 21일(5 ppm) 및 36일(7 ppm) 경과함에 따라 어느 일정 시점에서 황화수소 가스농도는 증가하지 않았으나 다른 필터여재에서는 일정한 경향은 보이지 않았다. 이상의 실험결과를 종합해 볼 때 무창 육성비육 돈사에서 Biofilter를 이용한 악취저감 효과를 확인할 수 있었다.

• 한국환경과학회:학술대회논문집
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• 한국환경과학회 1999년도 정기총회 및 봄 학술발표회 프로그램 The Korean Environmental Sciences Society
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• pp.173-175
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• 1999

• 한국산학기술학회:학술대회논문집
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• 한국산학기술학회 2003년도 춘계학술발표논문집
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• pp.331-333
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• 2003

The low-pH biofiltration system in laboratory experiments demonstrate defective performance for treating H2S. When leachate pH was in the range of 1.5 to 4, the biofilters in three different media removed H2S wi th efficiencies greater than 99％ while it was treated as a single contaminant. The posibility of using a single-stage low pH biofilter depends on its performance in treating VOCs. During Phase 2, a single-stage biofilter was effective for treating mixtures of H2S and toluene with toluene concentrations below 20ppm and leachate pH between 2 and 3.5. Biofiltration of xylene was ineffective when pH was lower than 1.5. The treatment system acclimated most slowly to benzene, and treatment of benzene was apparently subject to some competive inhibition from xylene and toluene. However. co-treatment was possible after some acclimation time. Xylene was not easily treated, with higher elimination capacities and no sign of competitive inhibition.

• Korean Chemical Engineering Research
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• 제48권3호
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• pp.382-390
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• 2010

본 연구에서는 광촉매반응기/폐가스 가습조(유동상호기 및 무산소조)를 포함한 바이오필터공정으로 이루어진 하이브리드시스템을 구축하여 퇴비공장 또는 공공시설에서 발생되는 황화수소, 암모니아 및 휘발성 유기화합물을 포함한 악취폐가스에 대한 처리효율을 제고하고 종합적인 적정 작업조건을 구축하였다. 악취가스(2 L/min)에 포함된 암모니아(300 ppmv)의 경우 광촉매반응기에서 약 22%가 제거되고, 폐가스 가습조에서 약 55%가 제거되고, 후 공정인 바이오필터에서 나머지인 약 23%가 모두 제거되었다. 악취가스에 포함된 톨루엔(100 ppmv)의 경우 광촉매반응공정에서 약 20%가 제거되고, 폐가스 가습조(유동상 호기 및 무산소조)에서 약 10% 제거되며 마지막 공정인 바이오필터에서 나머지 70% 모두가 제거되었다. 따라서 물에 용해도가 높은 암모니아의 경우에는 폐가스가습조에서 주로 제거되었고, 용해도가 낮은 톨루엔의 경우는 바이오필터에서 주로 제거되었다. 한편 황화수소(10 ppmv)는 광촉매반응공정에서 거의 처리되고 잔류 trace는 폐가스가습조에 용해되어서 바이오필터로 인입되는 가습된 feed에서 황화수소가 검지되지 않았다. 폐가스 가습조(유동상호기 및 무산소조)에서의 nitrate 농도는 무산소조에서 발생하는 탈질반응 때문에 무산소조 경우가 유동상호기조보다 약 3 ppm 정도 낮았다. 또한 폐가스가습조의 용존 암모니아 농도는 실험 시작부터 1,500~2,000 ppm 사이의 높은 값을 유지하였는데, 이는 폐가스 가습조 내부에 있는 용수에 포함된 염화암모늄 및 기타 암모니아성 질소원에 기인한다고 간주된다.

• Korean Chemical Engineering Research
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• 제50권1호
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• pp.149-154
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• 2012

바이오필터담체가 충전된 흡착칼럼 운전 시의 흡착 및 탈착거동에 대하여 조사하였다. 에탄올을 휘발성유기화합물(VOC)로서 함유하는 폐가스를 처리하기 위한 연속동적흡착 실험을 바이오필터공정과 같은 90% 이상의 상대습도에서 수행하였다. 에탄올 1,000 ppmv(or 2,050 mg ethanol/$m^3$)를 포함하는 폐가스 2 L/min을 흡착칼럼에 공급하였을 때에 흡착칼럼 출구에서의 파과점과 흡착평형에 이르는 시간은 1단 시료구에서 보다 각각 10배와 3배 만큼 지연되었다. 한편 에탄올 2,000 ppmv(or 4,100 mg ethanol/$m^3$)를 포함하는 폐가스의 경우에는 각각 9배와 3배 지연되었다. 이와 같이 흡착칼럼 출구에서 지연기간의 비는 공급농도와 무관하게 서로 거의 일치하였음이 관찰되었다. 또한 1단 시료구와 출구에서 비교한 유입폐가스의 에탄올농도의 10%를 보이는 탈착시간 지연비도 약 1.5배로서 거의 일치하였다. 한편 미생물활성과 멸균공정의 흡착평형에 대한 영향에 대하여 조사하였다. 멸균된 입상 활성탄으로 충전된 vial의 기상 에탄올 농도는 멸균되지 않은 입상 활성탄으로 충전된 경우와 거의 일치하였다. 그러나 퇴비(compost)나 입상 활성탄/퇴비 혼합물의 경우에는 멸균 안한 경우가 멸균한 경우보다 기상에서의 에탄올 농도가 현저하게 높았다.

• 한국환경과학회지
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• 제6권4호
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• pp.409-415
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• 1997

In order to Investigate the possibility as a simple technique of wastewater treatment for recirculating aquaculture system, the experiment by a biofilter unfit was carried out. The high and stable removal efficiency of nitrogen could be obtained by selecting the optimum recycle ratio and DO concentration. It was found that the proper combination of nitrifacation and denitrfication step in the reactor would be required for increasing the removal efficiency. The extent of nitrogen removal gradually decreased UO the rise of re- cycle ratio since the depression of denitrificatlon by the lack of hydrogen donor. The depression of nitrogen removal was overcome by increasing the CIN ratio In the wastewater. The extent of phosphorus removal was increased slightly with the increase of DO concentration and recycle ratio, but high removal efficiency was not observed. However, the extent of COD removal was not affected by recycle ratio and DO concentration and showed the stable removal of above 90%.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 2001년도 동계 학술대회 논문집
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• pp.387-392
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• 2001

• 한국환경과학회지
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• 제10권4호
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• pp.287-292
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• 2001

A packed bed of volcanic rock was used as deodorizing material to remove hydrogen sulfide($H_2$S) from air in a laboratory-scale column, and was inoculated with Thiobacillus sp. as $H_2S$ oxidizer. The effects of volcanic rock particle size distribution on system pressure drop were examined. Various tests have been conducted to evaluate the effect of $H_2S$ inlet concentration and CBCT(Empty Bed Contact Time) on $H_2S$ elimination. The pressure drop for particles of size range from 5.6 to 10 mm was 14 mm$H_2S$/m at a representative gas velocity of 0.25m/s. Biofilter using scoria and Thiobacillus sp. could get the stable removal efficiencies more than 99.9% under $H_2S$ inlet concentrations in the range from 30 to 1,100ppm at a constant gas flow rate of $15.2{\ell}$/min. $H_2S$ removal efficiencies greater than 99% were observed as long as EBCT was longer than 8sec at the 250ppm of $H_2S$ inlet concentration. When EBCT was reduced to 5.5 sec, $H_2S$ removal efficiency decreased by about 12 percent. The maximum $H_2S$ elimination capacity was determined to be 269g-$H_2S/m^3{\cdot}hr$.