• Journal of Energy Engineering
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• v.8 no.1
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• pp.150-158
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• 1999

본 연구는 저온플라즈마를 이용하여 배기가스중의 SOx와 NOx를 동시에 처리하는 공정을 개발하는 것으로서, 최적의 반응제 선정과 효율적인 공정의 구성을 위해 SOx, NOx와 반응제와 반응기구를 밝히고자 하였다. 실험은 1.0 N㎥/h의 모사가스를 이용한 기초실험과 20 N㎥/h의 실제 연소가스를 이용한 실험으로 진행되었으며, 반응제로는 NH3와 파리핀계 및 올레핀계 탄화수소를 사용하였다. NH3를 반응제로 한 SO2 제거반응은 비플라즈마 조건에서는 NH4HSO3, 플라즈마 조건에서는 (NH4)2SO4의 생성반응이었고, 두 조건 모두 높은 제거율을 나타냈다. 반응제를 사용하지 않은 플라즈마 조건에서 SO2는 환원반응이 일어나고 O2 농도의 증가는 역반응을 증가시키는 화학평형에 의해 SO2의 제거율이 감소되었다. 플라즈마 조건에서 NO는 O2농도가 낮은 경우는 NO의 환원반응이 주로 일어나고, O2 농도가 높을 경우는 산화반응이 지배적이었다. 올레핀계 탄화수소는 플라즈마 조건에서 NO 산화 반응에 탁월한 효과를 보였을 뿐만 아니라 SO2 제거에도 효과를 보여 최대 40%의 제거율을 나타냈으며, NH3의 사용을 줄일 수 있음을 확인하였다.

• Korean Journal of Fisheries and Aquatic Sciences
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• v.31 no.5
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• pp.622-630
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• 1998

Rotating Biological Contactor (RBC) was tested for the removal of total ammonia nitrogen (TAN) by using simulated aquaculture system. RBC performance was evaluated by controlling revolution rate of disk and hydraulic residence tile (HRT). The optimum revolution rate of disk was 4 rpm, As HRT of RBC was increased, TAN removal efficiency of RBC and TAN concentration of rearing water were increased. HRT for maintaining lowest TAN concentration of rearing water was 9.5 minutes and at that condition TAN concentration of rearing tank was $1.03 g/m^3$

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2008.11a
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• pp.517-521
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• 2008

Struvite의 최적 생성조건은 NH$_4$-N의 초기농도에 관계없이 모두 NH$_4^+$, PO$_4^{3-}$ 및 Mg$^{2+}$가 등몰비이고 pH 10.5이었다. Struvite 침전반응에서 NH$_4$-N 및 PO$_4$-P 제거율에 미치는 struvite seeding 효과는 습윤상태의 struvite를 seeding할 경우 그 효과가 거의 없었으나 건조된 struvite를 seeding할 경우 NH$_4$-N의 제거율은 증가되지만 PO$_4$-P의 제거율은 감소되는 경향을 나타냈다. 이는 건조과정에서 struvite의 NH$_4$-N가 휘산되어 소실되었기 때문이다. Mg와 P원으로서 struvite의 재이용을 위한 적정 건조온도는 100$^{\circ}C$ 이하였으며 그 이상 온도에서는 struvite가 $NH_4MgPO_4\cdot6H_2O$형에서 MgPO$_4$형으로 상전이점에 따라 struvite seeding에 의한 NE$_4$-N의 제거율이 현저히 감소되었다. 건조된 struvite는 초기 NH$_4$-N의 몰농도 대비 50%를 seeding할 경우 60% 이상의 NH$_4$-N를 제거하였으며, seeding량을 150%로 증가시킬 경우 90% 이상의 NH$_4$-N 제거율을 얻을 수 있었다. 그러나 struvite를 반복 재사용할 경우 재사용 횟수에 비례하여 NH$_4$-N의 제거율은 감소하는 경향을 보여 재사용 횟수가 제한적임을 알 수 있었다.

• Journal of the Korean Wood Science and Technology
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• v.32 no.2
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• pp.1-8
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• 2004

Heavy metals were removed from CCA- and CCFZ- treated wood using a brown-rot fungi Tyromyces palustris. The amount of effective elements extracted from treated woods was compared for different treatment methods. The relationship between the amount of heavy metals removed and concentrations of oxalic acid for treated wood was examined. Also, the relationship between mycelia weight and removal rate was examined. The removed quantity of heavy metal from treated wood according to fermentation methods was examined. The extraction amount of chromium and arsenic components increased with increasing oxalic acid concentration, but the extraction amount of copper did not improved much. A 287 mg of mycelia weight can remove chromium and arsenic over 60% in 3 g CCA chips and copper was also removed over 50%. The chromium, copper and arsenic were removed over 60% by shaking fermentation, the removal rate of copper by static cultivation was higher than that of shaking fermentation. The removal rate of chromium, copper and arsenic were 72%, 61% and 59% with air-lift bioreactor, respectively.

• Journal of Korean Society of Environmental Engineers
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• v.37 no.1
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• pp.7-13
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• 2015

In this study, the effective treatment reducing geosmin and dosage of PAC was suggested when taste & odor compounds flow in. The removal efficiency of geosmin was evaluated with types of chlorination. In case of low geosmin concentration below 25 ng/L, removal efficiency of geosmin was estimated at 46% by combined treatment of pre and intermediate-chlorination. But, in the exclusive intermediate-chlorination treatment, removal efficiency of geosmin was increased to 57%. In the medium geosmin concentration (25~79 ng/L), removal efficiency of geosmin was estimated at 59% by combined treatment. But, in the exclusive intermediate-chlorination treatment, removal efficiency of geosmin was increased to 87%. When high geosmin concentration above 80 ng/L flows in, removal efficiency of geosmin was estimated at 69% by combined treatment. However, in the exclusive intermediate-chlorination treatment, removal efficiency of geosmin was increased to 95%. Then, the exclusive intermediate-chlorination has an important effect on removal of geosmin. After correlation of geosmin concentration and dosage of PAC was analyzed, the coefficient of determination was estimated at 0.96. And, the proper PAC dosage chart was proposed. Also, at a initial occurrence of geosmin, when the combined treatment by intermediate-chlorination and PAC was applied, particle-bound geosmin should be removed continuously. Finally, it is proved that the combined treatment was effective to remove the geosmin by threshold levels as well as to reduce the dosage of PAC.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2008.11a
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• pp.503-506
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• 2008

질소제거 능력이 있는 Pseudomonas aeruginosa을 고분자물질인 PEG 에 포괄고정화하였으며 제조된 고정화 미생물을 이용하여 질소제거에 미치는 C/N비, 농도, 충진율, 탄소별 제거율을 검토한 결과 다음과 같은 결론을 얻었다. 1) C/N비 10이상이면 NH$_4$-N 와 NO$_3$-N의 동시 제거가 가능하였으며 2) 탄소 원으로는 glucose를 사용하였을 때 NH$_4$-N 와 NO$_3$-N의 동시 제거가 가능하였으나 methanol은 탄소원으로 사용할 수 없었다. 3) 저농도의 NO$_3$-N(50 mg/L)는 완전히 제거 가능하였으나 NH$_5$-N인 경우에는 초기 NH$_4$-N 100 mg/L에서 60%정도만 제거되었다. 4) 연속처리 결과 NH$_4$-N는 HRT 변동에도 불구하고 유출수 농도 변화가 거의 없었으나, 오히려 C/N비를 증가시키면 NH$_4$-N 제거 효율이 높았고, NO$_3$-N인 경우도 마찬가지로 C/N비를 증가시키면 NO$_3$-N 제거 효율이 높았다.

• Korean Journal of Fisheries and Aquatic Sciences
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• v.33 no.4
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• pp.367-372
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• 2000

A series of experiment was conducted to investigate the relationship between ammoia removal rate and ammonia loading rates in seawater filtering system using rotating biological contactor (RBC). In this experiment, RBC system was consisted of rotating polyvinyl film disks, which provided $12 m^2$ of total effective surface area in $0.075 m^3$ of volume. $NH_4Cl$ was added by $10{\~}150 g$ as a ammonia nitrogen source to determine ammonia removal rate in RBC system. Relationship between time required for ammonia removal (y: hour) and nitrogen inputted ($x: NH_4-N mg/l$) in RBC system was as followed: $y=3.51+7.76 lnx (r^2=0.936)$. At ammonia concentration $2 mg/l$, it took 10 hour for removal of ammonia in the RBC system. However, at ammonia concentration of $5 and 16.5 mg/l$, it took 16 and 27 hours, respectively. There was a decreasing tencency of an increasing ammonia in the rearing water. Finally, the ammonia removal rate in the RBC system increased with the rise of total ammonia concentration up to $16.5 mg/l$.

• Korean Journal of Environmental Agriculture
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• v.21 no.4
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• pp.274-278
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• 2002

Nitrate removal rate in three wetland cells was examined. The acreage of each cell was 150 $m^2$. They were a part of a stream water treatment demonstration system which was composed of two ponds and six wetland cells. Earth works far the pond-wetland system were finished from April 2000 to May 2000 and reeds were planted in the three cells in May 2001. Waters of Sinyang Stream flowing into Kohung Esturiane Lake located southern coastal area of Korean Peninsula were pumped into a primary pont Effluents from a secondary pond were funneled into the three cells. Volumes and water quality of inflow and outflow were analyzed from July 2001 through December 2001. Inflow and outflow averaged 20 $m^3/d$ and 19.3 $m^3/d$, respectively. Hydraulic retention time was 1.5 days. Average influent and effluent nitrate concentration was 2.30 mg/L, 1.75 mg/L, respectively. Nitrate removal rate in the three cells averaged 80.9 $mg/m^2/day$. Seasonal changes of nitrate retention rates were closely related to those of wetland temperatures. Full growth of reeds within a few years can develope litter-soil substrates beneficial to the denitrification of nitrate, which may lead to increases of the nitrate retention rates.

• Applied Chemistry for Engineering
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• v.19 no.5
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• pp.519-525
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• 2008

Biodegradation of toluene, styrene and hydrogen sulfide as model compounds of volatile organic compounds and odor from waste gas was investigated experimentally in a biotrickling filter. This study focussed on the description of experimental results with regard to operating conditions. The effect of varying $H_2S$ load rate and inlet concentration was investigated under autotropic and mixotropic environmental conditions. The $H_2S$ removal efficiencies of greater than 99% were achieved at $H_2S$ loads below $10g/m^3{\cdot}hr$ for each environment. It was observed that the maximum elimination capacity of mixotrophic filter was achieved a little greater than the one of autotrophic filter. The biofiltration of toluene and styrene in trickling bed was examined under different gas flow rates, load rates, and inlet concentrations. Below $40g/m^3{\cdot}hr$ of toluene loading, the elimination capacity and loading were identical and it was completely destroyed. In high loading of toluene, the biotrickling filter was operated at its maximum elimination capacity. In the inlet concentration of 0.2, 0.5, and $1.0g/m^3$, the maximum elimination capacity of toluene showed 40, 45, and $60g/m^3{\cdot}hr$, respectively. After a short adaptation period, it was demonstrated that the results of styrene in originally toluene adapted bioreactor was similar with the ones of toluene. However, the performance of filer for styrene is generally a little lower than for toluene. The operating conditions (including liquid flow rate etc.) allowing the highest removal efficiency should be determined experimentally for each specific case.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2005.11a
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• pp.72-74
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• 2005

활성탄/폴리우레탄을 접목하여 복합담체를 개발하고 이를 biofilter 담체로 충전하여 기상스틸렌의 제거 특성을 살펴본 결과, EBCT 200 sec일 때 유입농도 200 ppm의 고농도에서도 100%의 제거율을 보일 뿐만 아니라 스틸렌의 유입농도를 150 ppm으로 공급하여 EBCT를 75 sec 까지 낮추어 운전하여도 80% 이상의 높은 제거율을 보였다. 또한 본 연구의 활성탄/폴리우레탄 복합담체를 사용한 biofilter 운전에서 최대제거용량이 30.4 g/m$^3$/hr로 산정되어 비교적 높은 제거용량을 보여주었다. 이에 활성탄/폴리우레탄 복합담체를 충전한 biofilter 기술이 스틸렌을 효과적으로 제거할 수 있음을 보였다.