• 한국수산과학회지
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• 제26권5호
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• pp.502-509
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• 1993

Submerged filter process was used to evaluate the nitrifying efficiency of ammonia in the recycling water of marine aquatic culture system. The ammonia removal efficiency was achieved as high as $99\%$ at the hydraulic surface loading rate of up to $4.3{\ell}/m^2-day$. And the nitrite accumulation did not occur in the reactor even when the hydraulic surface loading rate of up to $36.8{\ell}/m^2day$ was applied. In the present study, the relationship between the effluent ammonia concentration and ammonia surface loading rate was formulated as an equation. The attachment rate of biofilm on the filter media at the ammonia surface loading rate of 62.3 and $311.7mg/m^2day$ was 15 and $55mg/m^2-day$, respectively, showing the linear relationship between the attachment rate and ammonia loading rates. Biofilm thickness and density of the filter media were found to be the function of the ammonia loading rate.

• KSBB Journal
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• 제4권3호
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• pp.241-245
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• 1989

Streptomyces erythreus의 포자를 다공성의 celite를 담체로 이용하여 미세구멍조직내에 흡착 후 배양하여 얻은 균사 증식 담체를 erythromycin의 발효에 응용하였다. 이때 균사체는 담체의 내부에서부터 포자가 발아하여 담체 표면으로 성장되어 나왔기 때문에 부착성이 강하고 매우 안정한 biofilm growth를 보여 주었다. 발효시 배지중의 com steep liquor의 양을 0.8g/L 첨가하여 인산원의 농도를 40mg $KH_2PO_4/L 정도로 하였을 때 항생제 비생산 속도는 최대값 2,898$\mu$g/g.cell.hr로서 인산원이 제한되지 않은 배지에서 얻은 비생산속도 557$\mu$g/g.cell.hr보다 약 4배의 증가효과를 보였다. 유동층 반응기를 이용한 연속 발효 공정에서도 인산원의 제한에 의하며 세포의 항생제 합성 활성은 약 600시간 이상 유지 되었다.

• Journal of Microbiology and Biotechnology
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• 제25권9호
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• pp.1547-1554
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• 2015

The potential of microalgae biofuel has not been realized because of the low productivity and high costs associated with the current cultivation systems. In this study, a new low-cost and transparent attachment material was tested for cultivation of a filamentous algal strain, Stigeoclonium sp., isolated from wastewater. Initially, the different materials tested for Stigeoclonium cultivation in untreated wastewater were nylon mesh, polyethylene mesh, polypropylene bundle (PB), polycarbonate plate, and viscose rayon. Among the materials tested, PB led to a firm attachment, high biomass (53.22 g/m², dry cell weight), and total lipid yield (5.8 g/m²) with no perceivable change in FAME profile. The Stigeoclonium-dominated biofilm consisted of bacteria and extracellular polysaccharide, which helped in biofilm formation and for effective wastewater treatment (viz., removal efficiency of total nitrogen and total phosphorus corresponded to ~38% and ~90%, respectively). PB also demonstrated high yields under multilayered cultivation in a single reactor treating wastewater. Hence, this system has several advantages over traditional suspended and attached systems, with possibility of increasing areal productivity three times using Stigeoclonium sp. Therefore, multilayered attached growth algal cultivation systems seem to be the future cultivation model for large-scale biodiesel production and wastewater treatment.

• Environmental Engineering Research
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• 제21권2호
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• pp.196-202
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• 2016

Membrane bioreactor (MBR) technology has previously been used by water industry to treat high salinity wastewater. In this study, an anoxic-oxic biofilm-membrane bioreactor (AOB-MBR) system has been developed to treat mustard tuber wastewater of 10% salinity (calculated as NaCl). To figure out the effects of operating conditions of the AOB-MBR on membrane fouling rate ($K_V$), response surface methodology was used to evaluate the interaction effect of the three key operational parameters, namely time interval for pump (t), aeration intensity ($U_{Gr}$) and transmembrane pressure (TMP). The optimal condition for lowest membrane fouling rate ($K_V$) was obtained: time interval was 4.0 min, aeration intensity was $14.6 m^3/(m^2{\cdot}h)$ and transmembrane pressure was 19.0 kPa. And under this condition, the treatment efficiency with different influent loads, i.e. 1.0, 1.9 and $3.3kgCODm^{-3}d^{-1}$ was researched. When the reactor influent load was less than $1.9kgCODm^{-3}d^{-1}$, the effluent could meet the third discharge standard of "Integrated Wastewater Discharge Standard". This study suggests that the model fitted by response surface methodology can predict accurately membrane fouling rate within the specified design space. And it is feasible to apply the AOB-MBR in the pickled mustard tuber factory, achieving satisfying effluent quality.

• 대한소아치과학회지
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• 제47권1호
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• pp.70-77
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• 2020

이 연구의 목적은 악궁 전반적으로 조사가 가능한 미백 LED를 이용하여 우식원성 Streptococcus mutans에 대한 광역동 치료의 효과를 알아보기 위한 in vitro 연구이다. S. mutans를 각각 두가지 다른 단계의 상태로 배양하였다. Planktonic 상태와 Hydroxyapatite disk와 CDC biofilm reactor를 5일간 사용하여 동적인 바이오필름 상태를 형성하였다. 20 μM 로 희석한 erythrosine을 5분간 전처리한후 가정용 미백기와 진료실 미백기를 사용하여 각 15분씩 광조사를 시행하였다. 실험 종료 후 각 실험군의 Colony Forming Unit를 측정하였으며 공초점 레이저 현미경를 이용하여 각 조건에 따른 광역동 치료 효과를 비교하였다. 실험 결과 S. mutans에 대한 aPDT효과는 control군과 비교시에 각각 플랑크토닉상태와 동적인 바이오필름 상태에서 모두 통계적으로 유의한 광역동 치료 효과가 나타났다(각각 p = 0.001, p = 0.002). 하지만 동적인 바이오필름 상태에서는 플랑크토닉 상태보다 광역동치료에 내성을 지녀 항미생물 효과가 떨어지는 양상이 관찰되었다. 진료실용 미백 LED와 가정용 미백LED는 유사한 항미생물 효과를 나타냈다. 구강악궁 전반적 조사가 가능한 미백용 LED는 우식의 원인이 되는 S. mutans 바이오필름에 유의한 광역동 치료의 효과를 나타냈으며, 이러한 결과는 치아 우식 예방으로의 광역동 치료의 임상적 적용 가능성을 제시한다.

• 대한소아치과학회지
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• 제47권2호
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• pp.188-195
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• 2020

이 연구는 새롭게 개발된 알카자이트 재료인 Cention N에 finishing처리를 한뒤에 표면 거칠기와 박테리아 부착에 대하여 조사하고자 함이다. 레진강화형 글래스아이오노머와 컴포짓트 레진, 알카자이트 재료를 원통형의 디스크 형태로 제작하였다(n = 48). 이 후 대조군과 3가지 카바이드버, 미세다이아몬드 버, 화이트스톤버의 피니싱 버에 따른 4가지 하위군으로 분류하였다. 표면 거칠기는 atomic force microscope으로 조사하였으며 표면관찰은 scanning electron microscope을 이용하여 진행하였다. 우식원성 미생물인 streptococcus mutans의 시편 부착을 위하여 CDC biofilm reactor를 사용하여 바이오필름을 배양한후 집락형성단위를 측정하였다. 레진과 Cention N의 아무처리 하지 않은 컨트롤 군의 표면 거칠기는 통계적으로 유의하게 피니싱 처리된 시편들보다 거칠었다. 하지만 표면 거칠기와 미생물 부착사이의 상관관계는 매우 약했다(PCC = 0.13). RMGI와 Cention N은 레진시편에 비해 미생물 부착이 적게 일어났다. Cention N은 피니싱만으로도 임상적으로 허용되는 수준인 0.2 ㎛ 이하의 거칠기를 보였으며 이온 방출 성질로 미생물 부착이 레진과 비교시 적은 것을 확인할수 있었다.

• 한국물환경학회지
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• 제23권5호
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• pp.776-780
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• 2007

A biofilm reactor packed with porous media was investigated for nitrogen removal of synthetic wastewater. The effect of different loading rates on the nitrification was sustained to be steady state with stable efficiency of 50~60% in the range of $0.0083{\sim}0.017gNH_4-N/gMLVSS{\cdot}day$ of F/MN ratio and $1{\sim}2kgNH_4-N/m^3{\cdot}day$ of media volumetric loading rate. However, nitrification efficiency was rapidly decreased to 25~30% as F/MN ratio and media volumetric loading rate were increased to the range of $0.025{\sim}0.034gNH_4-N/gMLVSS{\cdot}day$ and $3{\sim}4kgNH_4-N/m^3{\cdot}day$, respectively. Also the consumption rate of alkalinity was higher under 8 hours of HRT than unter 6 hours of HRT. Accordingly the influent loading rate variation by detention time with influent flow influenced more on the nitrification efficiency than the influent loading rate variation by the influent concentration did. The temperature effect on the nitrification showed 25% higher in summer than in winter as the results reported by other researchers who reported that the nitrification efficiency in biofilm showed 20% increase from 55% to 75% when the temperature was raised from $20^{\circ}C$ to $25^{\circ}C$. Denitrification with sulfur-media showed 90% removal efficiency under steady-state with no effect from the increase of influent concentration and empty bed contact time (EBCT) change such as EBCT was decreased from 8.4 hr to 4.3 hr and $NO_3-N$ loading rate was changed within the range of $0.1{\sim}0.4kgNO^3-N/m^3{\cdot}day$. Accordingly Denitrification with sulfur-media is feasible for post denitrification at the concentration less than $80mgNO^3-N/L$.

• 대한토목학회논문집
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• 제6권1호
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• pp.43-50
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• 1986

오염(汚染)된 원수내(原水內)의 biodegradable 한 유기물(有機物)의 제거(除去)를 위한 호기성(好氣性) 고정미생물막공법(固定微生物膜工法)의 적용가능성(適用可能性)을 확인하기 위하여 본(本) 연구(硏究)가 실시(實施)되었는데, 실험(實驗)은 파쇄(破碎)된 연탄재 또는 화강암을 매질(媒質)로 채운 충전상(充塡床)에 phenol과 무기성(無記性) 영양물질(榮養物質)을 용해(溶解)시켜 만든 합성원수(合成原水)를 주입(注入)함으로써 진행(進行)되었다. 실험결과(實驗結果)에 의하면 유입수(流入水)의 BOD 농도(濃度)가 50 mg/l 이하(以下)이고 체류시간(滯留時間)이 2.7 시간(時間)이었을 때 처리수(處理水)의 TBOD는 6 mg/l 이하(以下)로 유지되었으며, 처리수내(處理水內)의 SS가 응집(凝集)이나 여과(濾過) 등(等)의 재래식(在來式) 정수공법(淨水工法)에 의하여 제거(除去)될 수 있다는 점을 감안한다면 처리수(處理水)의 SBOD는 5 mg/l 이하로 유지될 수 있다. 처리수내(處理水內)의 SS가 낮은 BOD를 나타내었으므로 이들 SS가 대부분 부식질(腐植質)로 구성되었음을 알 수 있다. 이는 반응조내(反應槽內)의 미생물막(微生物膜)이 낮은 F/M 비 때문에 내호흡단계(內呼吸段階)에 있음을 뜻한다. 연구결과(硏究結果)에 따라, biodegradable한 유기물(有機物)로 오염(汚染)된 원수(原水)는 먼저 2~3시간의 체류기간을 가지는 호기성(好氣性) 고정미생물막반응조(固定微生物膜反應槽)로 전처리(前處理)함이 바람직스럽다.

• 한국환경과학회지
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• 제8권4호
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• pp.525-532
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• 1999

This study was conducted to evaluate capability of dyeing wastewater treatment for 3 type reactors. These reactors were Packed Bed Reactor(PBR), Fluidized Bed reactor(FBR) and Moving Media Complete Mixing Activated Sludge reactor(MMCMAS). Experiments of PBR and FBR were performed by various packing ratios and organic loading rates, experiments of MMCMAS were performed by various organic loading rates. In order to obtain ${SBOD}_5$ removal efficiencies of more than 90%, the F/Mv ratios of PBR, FBR, MMCMAS were 0.11 kgBOD/kgMLVSS$\cdot$d, 0.12 kgBOD/kgMLVSS$\cdot$d, and 0.37 kgBOD/kgMLSS$\cdot$d, respectively. So MMCMAS system which has more active microorganisms showed better capability of organic removal and also stronger dynamic and shock loadings than those of PBR and FBR. In PBR and FBR, the media packing ratio of 20% showed better performance of organic matters removal effciencies than 10% and 30%, but sludge production rate at media packing ratio of 30% was relatively lower than that of 10% and 20%. When more than 90% organic matters removal efficiency was obtained, the ratios of attached biomass to total biomass at PBR, FBR, MMCMAS were 89~99%, 87~98%, and 54~80%, respectively. The ratio of attached biomass to total biomass was low in MMCMAS. This was formation of thin biofilm due to shear force between rotaing disc and water. The average sludge production rates(kgVSS/kgBODrem.) of PBR, FBR and MMCMAS were 0.20, 0.29 and 0.54, respectively.

• 한국생물공학회:학술대회논문집
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• 한국생물공학회 2005년도 생물공학의 동향(XVI)
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• pp.247-251
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• 2005

This research was performed for developing of biological treatment process of odor gas such as MEK, $H_{2}S$, and toluene, which is generated from the food waste recycling process. To establish the operational conditions of odor gas removal by small-scale biofiltration equipment, it was continuously operated by using toluene as a treating odor object. When the odor treating microorganisms were adhered to fibril form biofilter, high removal efficiency over 93% was obtained by biofilm formation. At 400 ppm of inlet odor gas concentration and 10 sec of retention time, the removal efficiency was 76% and 93% in 1st stage reactor and 2nd stage reactor, respectively. However, the removal efficiency remained over 97% at the operational conditions above 15 sec of retention time.