• Journal of the Korean GEO-environmental Society
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• v.9 no.3
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• pp.35-43
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• 2008

This study was carried out to estimate the performance of modified sequencing batch reactor (SBR) process by the application of SBR process for small advanced wastewater treatment plant. Organic, nitrogen and phosphorus were able to remove in the unit reactor by SBR process and it would be able to select the suitable operation method. The plant was operated to achieve high performance with influent control, optimum anoxic/oxic condition using intermediate aeration method, and solid (sludge) /liquid (effluent) separation by modified decanter. The optimum operating mode was 3Cycles a day and intermediate input and aeration. Under these conditions, the treatment efficiencies were good with 60% of designed flow rate and low influent quality. When the influent concentrations of BOD and CODMn were 120.4 mg/L and 95.7 mg/L, respectively. The effluent concentrations of BOD and CODMn were 6.8 mg/L and 11.0 mg/L, respectively. The average removal efficiencies of BOD and CODMn were 94.4% and 88.5%, respectively. The removal efficiencies of T-N and T-P were 69.6% and 73.6%, respectively when the average T-N and T-P concentrations were 32.2mg/L and 4.65mg/L, respectively. The T-N and T-P removal efficiencies were slightly decreased to 58.8% and 68.5%, respectively in the winter season but its were also stable efficiencies. BOD, T-N and T-P were removed by 90%. 67% and 46% respectively in the first anoxic/oxic condition, in addition to T-P was removed by 70% in the second anoxic/oxic condition. From the results, modified sequencing batch reactor (SBR) process is suitable for small advanced wastewater treatment.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2006.05a
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• pp.342-346
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• 2006

본 연구에서는 음식물쓰레기를 고온호기성공정으로 처리시 수분증발량을 증대시키기위한 보조열량원으로 대두유를 첨가할 경우의 음식물쓰레기의 감량화 특성을 고찰하였으며, 그 결과는 다음과 같다. 음식물쓰레기부하를 50kg/$m^3$ d, 열량원으로 대두유를 0%, 5%, 10%, 15% 각각 첨가한 중량제거율에 근거한 음식물쓰레기 제거효율은 0% 첨가시는 94.5%, 5% 첨가시 97.6%, 10% 첨가시 91.7%, 15% 첨가시 87.2%로 나타났다. 대두유 첨가에 따른 열량비는 C/W비로 0.67, 1.52, 2.37, 3.21이었으며, 대두유를 5% 첨가한 경우의 음식물쓰레기 제거효율이 높은 것으로 판단되었고 고온호기성공정으로 음식물쓰레기를 처리할 경우 적정한 C/W비는 1.52인 것을 확인 할 수 있었다.

• Proceedings of the Korean Institute of Information and Commucation Sciences Conference
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• 2010.05a
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• pp.795-797
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• 2010

습식 식각은 식각용액으로서 화학용액을 사용하는 공정으로 반응물이 기판표면에서 화학반응을 일으켜 표면을 식각하는 과정이며, 표면결합의 제거를 위한 식각연마와 폴리싱을 위한 식각, 그리고 구조적 형상 패턴등이 있다. 여기서 화학용액은 산화제 또는 환원제 역할을 하는 혼합용액으로 구성된다. 습식 식각 시 수${\mu}m$의 해상도를 얻기 위해서는 그 부식액의 조성이나, 에칭시간, 부식액의 온도 등을 고려하여야 한다. 또한 습식 식각 후 포토 레지스트를 제거하는 과정에서 포토 레지스트를 깨끗이 제거해야 하며, 제거공정 자체가 a-Si:H 박막을 부식 하지 않을 조건으로 행하여야 한다. 포토레지스트 제거 후 잔류 포토 레지스트를 제거하기 위해서 본 실험에서는 RCA-I 세척 기법을 사용한 후 D.I 로 린스 하였다. 본 실험에서 사용한 금속은 Cr, Al, ITO 로 모두 DC sputter 방법을 사용해서 증착하여 사용하였다. Cr박막은 $1300\AA$ 정도의 두께를 사용하였고, ITO (Indium Tin Oxide) 박막은 가시광 영역에서 투명하고 (80% 이상의 transmittance), 저저항 (Sheet Resistance : $50{\Omega}/sq$ 이하) 인 박막을 사용하였으며, 신호선으로 주로 사용되는 Al등의 증착조건에 따른 wet etching 특성을 조사하였다.

• Journal of environmental and Sanitary engineering
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• v.16 no.2
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• pp.71-78
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• 2001

본 연구는 폐수 중 함유된 고농도의 LAS를 제거하기 위해 $FeSO_4$를 이용한 응집, 펜톤산화, 펜톤 공정 전.후에 응집공정을 조합시킨 Coagu-oxidation 및 Renton's Coagulation을 이용하여, 처리 시 최적 조건을 도출하고, 효율적인 화학적 처리방법을 검토하기 위해 수행되었다. 연구로부터 얻어진 결론은 다음과 같다. 응집공정은 pH 8, 응집제의 주입량 200mg/L인 조건에서, 펜톤산화는 pH 3, $H_2$$O_2$에 대한 ${Fe^2}^{+}$의 비가 1:1인 조건에서 최적효율을 보였다. Fenton's Coagulation 처리 시 LAS의 개환율은 높아졌고, 주입된 LAS농도의 73~96%가 제거되어 4가지 처리 방법 중 가 장 좋은 처리효율을 보였다. 따라서, LAS의 생물학적 처리 시 거품 및 부산물 생성 등에 의해 저해작용을 감안한다면, LAS가 다량으로 함유한 산업 폐수에서 화학적 처리방법의 도 입이 적절할 것으로 생각되며, 이들 중 Fenton's Coagulation을 유용하게 적용될 수 있을 것으로 판단된다.

• Microbiology and Biotechnology Letters
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• v.33 no.2
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• pp.136-141
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• 2005

A bench-scale feasibility study was conducted with solid farming feed to evaluate a treatment process for microbiological removal of nitrogen (N) and phosphorus (P). Strains, Bacillus sp. CK-10 and Bacillus sp. CK-13, were originally isolated from water samples of shrimp farming pond. Simultaneous removal of N/P in marine media was monitored in the co-cultures, CK-10 and CK-13. As the results, $400\;{\mu}M\;NH^{+}_4$ and $400\;{\mu}M\;NO^{-}_2$ were eliminated within 12 hours and $NO^{-}_3$ within 36 hours, and $500\;{\mu}M\;PO^{-3}_4$ was completely disappeared within 36 hours from the media. Cultures of CK-10 and CK-13 were applied for removal of N/P leached from shrimp farming fred. HPAEC-PAD system was used to analyze sugars in farming feed, resulting in resolution of various sugars including glucose, galactose, galatosamine, mannose, and fucose. $0.2\%$ (w/v) Pulp densities of the farming feed contained approximately $33.3\;{\mu}M\;NH^{+}_4,\;12.9\;{\mu}M\;NO^{-}_2.\;81.5\;{\mu}M\;NO^{-}_3\;and\;248\;{\mu}M\;PO^{-3}_4$ which could dissolved within 72 hours of leaching in aqueous solution followed by bacterial removal. Complete bacterial removal of N/P was achieved within 84 hours at $0.2\%$ of the feed in co-cultures, whereas single cultures removed to incompletion of N/P during the incubation period. This work demonstrated that test cultures, CK-10 and CK-13 showed effective removal of N/P derived from shrimp farming feed.

• Korean Journal of Environmental Agriculture
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• v.29 no.3
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• pp.232-238
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• 2010

The objective of this study was to investigate a small sewage treatment system. This system was developed to improve a nitrogen and phosphorus removal efficiency and generate less solid using upflow septic tank(UST) - aerobic filter(AF) system. The UST equipped with an aerobic filter, the filter was fed with both raw sewage and recycled effluent from the UST to induce the denitrification and solid reduction simultaneously. Overall removal efficiencies of COD and total nitrogen(TN) were above 96% and 73% at recycle ratio of 200%, respectively. Critical coagulant dose without the biochemical activity was found to be 40 mg/L. Removal efficiency of total phosphorus(TP) in influent was above 90% by chemical and biological reactions. Although the phosphorus concentration was low under the high alkalinity in raw sewage, the pH value was unchanged by the coagulant dose.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.14 no.2
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• pp.970-976
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• 2013

An evaluation of the organic matter removal efficiency showed high removal efficiencies of 91.1~96.3% and 91.4~97.5% for TCODcr and TBOD5, respectively, for 9hr or longer of HRT. However, the removal efficiencies decreased to 86.9~90.5% and 88.0~90.9%, respectively for 6hr of HRT. $NH_3$-N showed a high removal efficiency of 95% or higher for 9hr or longer of HRT. The total nitrogen removal efficiency was 67.6~76.7% for 9~12hr of HRT, and it decreased to 50% for 6hr of HRT, which seems to be due to the insufficient carbon source required for denitrification. The T-P removal efficiency was 32% on average. To comply with the legal standards, a chemical phosphorus removal process is needed after the reactor.

• Journal of the Korea Organic Resources Recycling Association
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• v.21 no.2
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• pp.63-70
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• 2013

Experiments in a pilot-scale hybrid multi-stage unit system (HMUS) combination of ATAD and EGSB followed by SBR process for pig slurry treatment were conducted to demonstrate the feasibility of using autothermal thermophilic aerobic digestion (ATAD) and expended granular sludge bed (EGSB) followed by sequencing batch reactor (SBR) system. Contaminants in pig slurry with high organic matter, nitrogen (N) and phosphorus (P) content were completely removed in the combined process. The highest removal rate for CODcr among contaminants in the feed pig slurry was attained by about 43.3% in ATAD unit process. Also TS removal rate of 96.5% was attained and the highest in the next coagulation unit process. The highest removal rate of CODcr under operating parameter conditions of OLR(organic loading rate), 3-6Kg $COD/m^3{\cdot}day$ and line velocity, 1.5-4m/h was earned at 3days of HRT. The disinfection of pathogens was effective at 50,000mg/L of TS in ATAD unit process. Biogas production per organic removal was $2.3{\sim}8.5m^3/kgTS{\cdot}d$ (average $5.2m^3/kgTS{\cdot}d$) in EGSB unit process. The average removal rates of CODcr 71.7%, TS 64.1%, TN 45.9%, and TP 50.4% were earned in the intermittent aeration SBR unit process.

• Journal of Korean Society of Environmental Engineers
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• v.39 no.1
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• pp.40-49
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• 2017

In this study, we have made the annual total phosphorus (TP) mass balance diagrams for I wastewater treatment plant by utilizing the data of flow rate and TP of each process and tried to choose the optimum unit process empirically for phosphorus recovery. For the applicability evaluation, we have suggested several quantitative indices of flow rate, TP concentration, TP load and SS. Based on the analyses of TP mass balance, it became clear for reducing TP load of the wastewater treatment plant that it is efficient to recover phosphorus from the side stream in which the amount of flow rate is just 1/16, but TP concentration and load are 78 and 4.8 times larger than those of the influent of the plant. After the detailed applicability evaluation for the side stream, it could be concluded that the unit process of waste activated sludge thickener supernatant or dehydration filtrate are appropriate. Meanwhile, we did fundamental experiments utilizing the dewatering filtrate with TP concentration of 141.5 mg/L. After adjusting pH 10 and $Ca^{2+}$ concentration 250, 500, 1000 mg/L, it was stirred slowly. As a result, the $PO_4-P$ and TP removal efficiencies were above 95 percent; the results of the experiment imply the applicability of phosphorus recovery process in a wastewater treatment plant strongly.

• 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.