• Title/Summary/Keyword: Pilot plant

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Application of Ceramic MF Membrane at the Slow Sand Filtration Process (완속모래여과 공정에서 세라믹 MF 막의 적용)

  • Choi, Kwang-Hun;Park, Jong-Yul;Kim, Su-Han;Kim, Jeong-Sook;Kang, Lim-Seok
    • Journal of Korean Society of Environmental Engineers
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    • v.35 no.12
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    • pp.877-882
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    • 2013
  • The application of ultrafiltration (UF) and microfiltration (MF) membranes has been increased for drinking water purification. The advantages of UF/MF membrane process compared to conventional treatment processes are stable operation under varying feed water quality, smaller construction area, and automatic operation. Most membrane treatment plants are designed with polymeric membranes. Recently, some studies suggested that the process of treating surface water with ceramic membranes is competitive to the application of polymeric membranes. Higher water flux, less frequent cleaning, and much longer lifetime are the advantages of ceramic membrane comparing to polymeric membrane. Therefore, this research focused on the application of ceramic MF membrane pilot plant at the slow sand filtration plant. The ceramic membrane pilot plant has three trains that used raw water and sand filtered water as a feed water, respectively. For optimizing the pilot plant process, the coagulation with PACl coagulant was used as a pretreatment of ceramic membrane process. In addition, CEB (Chemical Enhanced Backwash) process using $H_2SO_4$ and NaOCl was used for 1.5 days, respectively. The experimental results showed that applying the optimum coagulant dose before membrane filtration showed enhancing membrane fluxes for both raw water and sand filtered water. Also, when using raw water as a feed of membrane, minimum fouling rate was 2.173 kPa/cycle with 25 mg/L of PACl and when using sand filtered water, the minimum fouling rate was 0.301 kPa/cycle with 5 mg/L of PACl.

Evaluation of Air Quality in the Compost Pilot Plant with Livestock Manure by Operation Types (축분 퇴비화시스템 운용방식에 따른 실내 대기오염 평가)

  • Kim, K.Y.;Choi, H.L.;Ko, H.J.;Kim, C.N.
    • Journal of Animal Science and Technology
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    • v.46 no.2
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    • pp.283-294
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    • 2004
  • Air quality in the livestock waste compost pilot plant at the Colligate Livestock Station was assessed to quantity the emissions of aerial contaminants and evaluate the degree of correlation between them for different operation strategies; with the ventilation types and agitation of compost pile, in this study. The parameters analyzed to reflect the level of air quality in the livestock waste compost pilot plant were the gaseous contaminants; ammonia, hydrogen sulfide, and odor concentration, the particulate contaminants; inhalable dust and respirable dust, and the biological contaminants; total airborne bacteria and fungi. The mean concentrations of ammonia, hydrogen sulfide, and odor concentration in the compost pilot plant without agitation were 2.45ppm, 19.96ppb, and 15.8 when it was naturally ventilated, and 7.61ppm, 31.36ppb, and 30.2 when mechanically ventilated. Those with agitation were 5.50ppm, 14.69ppb, and 46.4 when naturally ventilated, and 30.12ppm, 39.91ppb, and 205.5 when mechanically ventilated. The mean concentrations of inhalable and respirable dust in the compost pilot plant without agitation were 368.6${\mu}g$/$m^3$ and 96.0${\mu}g$/$m^3$ with natural ventilation, and 283.9${\mu}g$/$m^3$ and 119.5${\mu}g$/$m^3$ with mechanical ventilation. They were also observed with agitation to 208.7${\mu}g$/$m^3$ and 139.8${\mu}g$/$m^3$ with natural ventilation, and 209.2${\mu}g$/$m^3$ and 131.7${\mu}g$/$m^3$ with mechanical ventilation. Averaged concentrations of total airborne bacteria and fungi in the compost pilot plant without agitation were observed to 28,673cfu/$m^3$ and 22,507cfu/$m^3$ with natural ventilation, and 7,462cfu/$m^3$ and 3,228cfu/$m^3$ with mechanical ventilation. They were also observed with agitation to 19,592cfu/$m^3$ and 26,376cfu/$m^3$ with the natural ventilation, and 18,645cfu/$m^3$ and 24,581cfu/$m^3$ with the mechanical ventilation. It showed that the emission rates of gaseous pollutants, such as ammonia, hydrogen sulfide, and odor concentration, in the compost pilot plant operated with the mechanical ventilation and with the agitation of compost pile were higher than those with the natural ventilation and without the agitation. While the concentrations of inhalable dust and total airborne bacteria in the compost pilot plant with the natural ventilation and with the agitation, the concentrations of respirable dust and total airborne fungi in the compost pilot plant with the mechanical ventilation and agitation were higher than those with the natural ventilation and without the agitation of compost pile. It was statistically proved that indoor temperature and relative humidity affected the release of particulates and biological pollutants, and ammonia and hydrogen sulfide were believed primary malodorous compounds emitted from the compost pilot plant.

Removal of Odor and THM from the Raw Water of Daecheong Dam (대청호 원수내 냄새 및 THM 제거방안 연구)

  • Jeon, Hang-Bae;Yun, Gi-Sik
    • Journal of Korea Water Resources Association
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    • v.30 no.3
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    • pp.235-245
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    • 1997
  • A pilot scale study for removing odor and trihalomethane formation potential (THMFP) was investigated in the standard water treatment plant equipped with ozone oxidation and granular activated carbon (GAC) adsorption processes. The removal efficiency of dissolved organic carbon (DOC) in the pilot scale standard water treatment process (PSWTP) was about 25%, however, no more removal in the ozone oxidation process. On a GAC after 30 days operation, DOC removal efficiency was about 75%. Odor removal efficiency was about 30% in PSWTP, 60% in ozone oxidation, and almost complete in well as DOC. Mid-1 and 2 that showed breakthrough in odor inducing material as well as DOC. Mid-1 and 2 chlorination was able to reduce trihalomethanes (THM) by 25% compared to prechloringation, while postchlorination alone could reduce them by 30%.

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Complex odor removal in pilot-scale biofilter with microorganisms immobilized on polymer gel media (미생물 포괄고정화 담체를 적용한 파일럿 스케일 바이오필터에서의 복합악취 제거)

  • Kim, Sun-Jin;Kim, Tae-Hyeong;Lee, Yun-Hee;Jang, Hyun-Sup;Song, Ji-Hyeon;Hwang, Sun-Jin
    • Journal of Korean Society of Water and Wastewater
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    • v.25 no.5
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    • pp.741-750
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    • 2011
  • A pilot-scale biofilter was constructed to discover degradation characteristics of the complex odor discharged from Ansan wastewater treatment plant. Candida tropicalis for volatile organic compounds, sulfur oxidizing bacteria(SOB) for hydrogen sulfide, and bacteria extracted from feces soil were immobilized on a polymer gel media. According to this study, the EBCT was varied from 36 sec to 18 sec. Toluene was removed as 80% along the variations, but it was recovered as 100% within 1 week. All benzene and xylene were removed during the operation while the efficiency of hydrogen sulfur was temporary decreased at 18 sec of EBCT, thereafter it was recovered to 100% within a week. The maximum elimination capacities of the benzene, toluene, xylene, and hydrogen sulfur were 6.6 g/$m^{3}$/hr, 31.7 g/$m^{3}$/hr, 7.8 g/$m^{3}$/hr, and 133.6 g/$m^{3}$/hr, respectively. There were merits on removal both organic and inorganic complex odor using the pilot-scale biofilter embedded with microorganisms immobilized on polymer gel media.

Removal of Ammonia Nitrogen and Reduction of THMs in Low Temperature by BAC Pilot Plant (BAC Pilot Plant 를 이용한 겨울철 암모니아성 질소 제거 및 THMs 변화)

  • Kang, Eun-Jo;Seo, Young-Jin;Lee, Won-Kwon;Chun, Pyoung-Hee;Lee, Ji-Hyung;Yoon, Jung-Hyo;Kim, Dong-Youn
    • Journal of Korean Society of Water and Wastewater
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    • v.9 no.4
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    • pp.107-114
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    • 1995
  • The raw drinking water quality is getting worse because of the winter drought and the conventional treatment system is'nt suitable to obtain the satisfied quality of water. So, the advanced water system, BAC(Biological Activated Carbon) process is said to be effective to remove dissolved organics and ammonia nitrogen. In our study, the BAC pilot plant using Nak-dong river water is tested in low temperature. Following results are found from the study. The ammonia nitrogen removal rate of BAC system using wood-based carbon (PICABIOL) was 99% in $6^{\circ}C$ temperature. Chlorine dosage in wood-based BAC effluent was reduced to 67% of that in sand filtered wate. It resulted from the removal of ammonia nitrogen. Also, THM formed by chlorine addition in wood-based BAC effluent was decreased to 65% of that in sand filtered water. In the case of dual-filter, the removal efficiency of ammonia nitrogen was increased 30% more than in conventional sand filter. According to this result, the ammonia nitrogen load to BAC system could be lessened by the use of dual-filter.

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The Characteristics with HRT Variation on InSub Pilot Plant for Advanced Sewage Treatment

  • Kang, Jin-Young;Huh, Mock
    • Environmental Engineering Research
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    • v.14 no.3
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    • pp.174-179
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    • 2009
  • The InSub system(applied for a patent) was developed, as it combined the indirectly aerated submerged biofiltration(InSub) reactor and Anaerobic/ Anoxic reactor. This system which can eliminate organism and nutrient materials at the same time, which is safe and economical to be maintained and managed is more simple process than the complicated existing biological advanced sewage treatment system. The most suitable HRT of this study showed 9 hours. As looking into the effluent concentration and removal efficiency of each item at 9 hours of HRT, each effluent concentration for $SS,\;BOD5,\;COD_{Mn},\;and\;COD_{Cr}$ was 1.46 mg/L, 7,09 mg/L, 9.84 mg/L and 16.42 mg/L. And their removal efficiency was 96.98%. 90.59%, 77.18% and 83.92%, respectively. Each effluent concentration of T-N and T-P was 10.42 mg/L and 1.04 mg/L. Their removal efficiency was 73.38% and 61.62%, respectively. This pilot plant experiment(the state was without the internal recycling.) followed a variety of HRT. The results confirmed that it was to be advanced sewage treatment system with high efficiency when it combined with the internal recycling.

The study for Biological nutrient removal of High-strength nitrogen loading rate using B3 pilot plant (B3 Pliot plant를 이용한 고농도 질소부하에서의 고도처리에 관한 연구)

  • Eorn Tae-Kyu;Han Dong-Yueb;Kim Boo-Gil
    • Journal of Environmental Science International
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    • v.14 no.8
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    • pp.771-775
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    • 2005
  • The purpose of this research was to investigate applicative possibility of field. Pilot-scale experiments were conducted, at outdoor temperature, HRT l0hour, IR(Internal Recycle) $150\%$ and used $2.8m^3$ Reactor. External carbon source was varied 80 to 120 mg/L. When External carbon source and Alkalinity were injected to the B3 pilot plant, the removal efficiencies of COD and BOD were not decreased. Nitrification rate were 5.95, 5.40, 4.08 $mgNH_4^+-N/gSS/d$ during operation periods and denitrification rate was $3.l2mgNO_3^--N/gSS/d.$ When we surveyed the relationship between loading rate of nitrogen and nitrogen removal quantity, this data was 0.949, B3 process will be possible application process of field.

Field application on biological treatment process for removing 1,4-dioxane (1,4-dioxane 제거를 위한 생물학적 처리공정의 현장 적용성 검토)

  • Park, Doori;Lee, Kanghun;Jun, Moonhwee;Yeom, Icktae
    • Proceedings of the Korea Water Resources Association Conference
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    • 2015.05a
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    • pp.283-283
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    • 2015
  • 1,4-dioxane은 페인트, 광택제 및 코팅제의 제조시에 첨가되는 화학물질로 인간에 대한 발암 가능성과 수중에서의 지속성으로 인해 EPA priority pollutant로 지정되어 있다. 이에 최근 고도산화법을 이용한 처리가 계속적으로 연구되고 있으며, UV/$H_2O_2$ 공법을 통하여 수계에서 발견되는 난분해성 유기 오염물의 제거가 효과적인 것으로 밝혀졌다. 하지만 고도산화공정(AOP)은 다량의 에너지 소모와 산화제 투여로 인한 높은 운전비용이 현실적인 적용에 장애가 되고 있다. 한편 상대적으로 저렴한 비용으로 1,4-dioxane을 처리할 수 있다는 장점으로 인하여 생물학적 분해에 대한 많은 연구가 진행되어 왔다. 하지만, 1,4-dioxane에 대한 많은 연구들이 주로 분해미생물의 분리동정 및 회분식 분해특성에 대한 연구들 위주로 보다 실질적인 연속적 처리반응조의 운전결과들은 거의보고 되지 않고 있다. 본 연구는 Lab scale 연속처리반응조의 장기운전 후 pilot plant 현장적용에 앞서 인공폐수와 합성폐수에서의 분해효율 비교 회분식 실험을 통해 합성폐수내 생물학적 분해에 영향을 미치는 inhibitor의 영향을 확인하였으며, 미생물의 배양 조건에 따른 분해효율 비교 회분식 실험과 modeling을 통하여 현장운영 효율을 예측하였다. 이를 반영하여 추후 진행예정인 pilot plant의 현장 적용성 검토 및 최적 설계인자 도출, 장기운전에서의 효율성 증대를 목적으로 한다.

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Thermal Analysis of a Cold Box for a Hydrogen Liquefaction Pilot Plant with 0.5 TPD Capacity (0.5 TPD 급 수소액화 파일럿 플랜트의 콜드박스 열해석)

  • KIM, HYOBONG;HONG, YONG-JU;YEOM, HANKIL;PARK, JIHO;KO, JUNSEOK;PARK, SEONG-JE;IN, SEHWAN
    • Transactions of the Korean hydrogen and new energy society
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    • v.31 no.6
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    • pp.571-577
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    • 2020
  • Thermal analysis was performed for a cold box of a hydrogen liquefaction pilot plant with 0.5 ton/day capacity. The pilot plant has adopted a hydrogen liquefaction process using two-stage helium Brayton cycle with precooling of liquid nitrogen. The cold box for hydrogen liquefaction has generally vacuum insulation but inevitable heat invasion by conduction and radiation exists. The heat loads were calculated for cold box internals according to multilayer insulation emissivity. Total heat load of 181.7 W is estimated for emissivity of 0.03 considered in field condition.