• 제목/요약/키워드: Dual-media filtration

검색결과 17건 처리시간 0.026초

일유량 변동에 따른 여과수질 악화에 대처하기 위한 최적 여재구성에 관한 연구 (The Optimal Composing the Filter-Bed for Coping with Daily Flow-Rate Fluctuation for the Performance of Sand Filtration Process)

  • 박동학;박노석;김성수;배철호;정남정;최승일
    • 상하수도학회지
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    • 제21권4호
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    • pp.485-491
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    • 2007
  • The fluctuation of inlet flow to a water treatment plant makes a serious problem that it can change the filtration rate abruptly, and ultimately occur the breakthrough of the detained particles inside filter media. Also, since it takes very short time (about 10 minutes) for the surface wave occurred from the fluctuation of inlet flow to reach the filtration process, it is impossible to control the filtration rate stably. Therefore, this study was conducted to evaluate the effect of daily flow-rate fluctuation on the performance of sand filtration process, and to suggest the dual media composition for coping with that effect. Comparative column tests have been carried out for various dual media (sand and anthracite) compositions. From the results of column tests, dual media, especially in the case of sand 45cm/anthracite 30cm, is more effective to cope with the effect of flow-rate fluctuation on the performance of filtration than single media (only sand). In addition, irrespective of dual media composition, managing ability to cope with that fluctuation tends to be weak at the end of allowable filtration duration time,

정수처리장 사여과지의 이단이중여과재 시스템으로의 개량 (Improvement of Rapid Sand Filtration to Two Stage Dual Media Filtration System in Water Treatment Plant)

  • 우달식;김준언;황병기;채수권;조관형
    • 한국환경과학회지
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    • 제23권4호
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    • pp.737-742
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    • 2014
  • This study aimed for evaluating the applicability of the two stage dual media filtration system in field water treatment plant. The field plant of two stage and dual media filtration system was operated for 2 months. Average iron concentrations of the settled water, existing filtered water and second stage filtered water was 0.041 mg/L, 0.007 mg/L and 0.005 mg/L, respectively. Removal efficiency of iron concentration in the second stage is appropriately 35% more than in existing filtered water. Also removal efficiency of residual chlorine in the dual media filtration system is relatively 42.3% more than in existing filtered water due to adsorption of activated carbon, but the removal of ammonia nitrogen by adsorption is insufficient. Average concentrations of THM and chloroform in the settled water are 0.033 mg/L, 0.026 mg/L, respectively and in existing filtered water are 0.023 mg/L and 0.023 mg/L. Average concentrations of THM and chloroform in the dual media filtration system are 0.008 mg/L and 0.013 mg/L. Therefore removal efficiency of THM concentration in second stage is more than 66.4% in existing filtrated water. Also removal efficiency of chloroform in the dual media filtration system is more than 50.0% in existing filtered water because of the adsorption of activated carbon. In this case backwashing period in dual stage system is 4~5 days, but in existing filtration system is 1~2 days.

정수처리장내 급속모래 여과지의 이단복합여과시스템으로의 개량 (Improvement of Rapid Sand Filtration to Two Stage Dual Media Filtration System in Water Treatment Plant)

  • 우달식;황규원;김준언;황병기;조관형
    • 한국환경보건학회지
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    • 제37권2호
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    • pp.141-149
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    • 2011
  • This study aimed for developing a two stage dual media filtration system. It has a sand and activated carbon layer above the under-drain system, and a sand layer above the middle-drain system for pretreatment. When retrofitting an old sand filter bed or designing a new one, this technology can substitute the existing sand filter bed without requiring a new plant site. The removal rate of total particle is 93, and 3~7 ${\mu}m$ and 5~15 ${\mu}m$ particles are all 97%. These high removal efficiencies of each pollutant due to adsorption and biological oxidation in activated carbon filter layer. The best backwashing method of two stage dual media filtration system is ascertained by air injection, air + water injection and water injection sequence. In this study, a pilot plant of two stage and dual filtration system was operated for 4 months in water treatment plant. The stability of turbidity was maintained below 1 NTU. The TOC, THMFP and HAAFP were removed about 90% by two stage and dual media filtration system, which is almost 2 times higher than existing water treatment plant.

심층여과지의 여층구성에 따른 여과특성 비교 (Characteristics of Depth Filtration for Various Filter-Bed Configurations)

  • 안종호;윤재흥
    • 한국수자원학회논문집
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    • 제34권5호
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    • pp.459-472
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    • 2001
  • 모형실험장치를 이용하여 심층여과지에 대한 여층구성별 여과효율 평가를 통해 여과지 설계시의 여층구성에 대한 기초자료를 제공하는 것이 본 연구의 목적이다. 여과지속시간에 따른 손실수두 발달특성을 보면 여과초기의 수두손실은 이중여재 여과지가 높지만 탁질 억류에 의한 수두손실의 증가는 완만하여 여과속도 180 m/day의 동일한 여과속도를 적용하였을 경우, 조림심층 모래여과지에 비해 단위정수생산량이 30-40% 정도 증대되는 것으로 나타났다. 여과수질은 각각 여과속도 180 m/day, 240 m/day로 운전한 결과 여과속도에 관계없이 모두 0.1 NTU 이하를 나타내어 만족하는 여과수질을 보였다. 그러나 여과초기 탁질 누출 특성을 보면 상대적으로 조립심층 모래여과지의 누출 경향이 크게 나타났고, 여과속도 240 m/day로 증대됨에 따라 그 경향은 보다 뚜렷하게 나타났다.

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여과 성능향상을 위한 이단이층 복합여과시스템의 공정선정 연구 (A Study on the Process Selection for Two-stage and Dual Media Filtration System for Improving Filtration Performance)

  • 송시범;조민;남상호;우달식
    • 상하수도학회지
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    • 제21권2호
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    • pp.203-214
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    • 2007
  • This study aimed at researching the process selection for two-stage and dual media filtration system, as a technology substituting the existing sand filter without expanding the site when retrofitting an old filter bed or designing a new one. In order to select the process for optimum complex filtration system, three running conditions have been tested. Test results demonstrated that Run 3 in which the 1st stage was filled with anthracite and coarse sand, and the 2nd stage was filled up with activated carbon and fine sand reduced the head loss and the load of turbidity substances. Also, Run 3 showed better performance in removing TOC, particle counts, THMFP and HAAFP, compared to other two conditions. 99 % of Cryptosporidium was removed. Bisphenol-A was rarely removed from the 1st stage of coarse sand and 2nd stage of fine sand, but 99 % of it was removed from the 2nd stage of activated carbon. In conclusion, when it is required to retrofit an old rapid filter bed or design a new one for the purpose of improving filtration performance, the following two-stage and dual media filtration system is suggested: the 1st stage of filter bed needs to be filled up with coarse sand to remove turbidity as the pretreatment for extending duration of filtering, the top part of 2nd stage needs to be filled up with granular activated caron to remove dissolved organic matters and others as the main process, and finally the bottom part of 2nd stage needs to be filled up with fine sand as the finishing process.

정수처리를 위한 여과지의 역세척에 관한 연구 (A Study on Backwashing of Granular Fiters Used in Water Treatment)

  • 이정택;안종호;최근호
    • 상하수도학회지
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    • 제13권3호
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    • pp.61-72
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    • 1999
  • To obtain the experimental data for design and operation of actual filtration processes, a sand filter and three kinds of dual media filters in pilot-plant scale were operated in this study. We analyzed the effect of filter medium composition on the filter performance and the effects of backwash water flow rates, length of stream line and air flow rate on the filter backwash efficiency. We also compared the efficiencies of the combined air-water backwashing and the water backwashing in dual media filters. As the backwash water flow rates or the length of stream line increased, the final turbidity of backwash water was decreased and the filtration duration time after backwash was increased. In the case of the combined air-water backwashing, the backwash water quantity needed for backwashing the dual media filters could be decreased. The total volume of filtered water for the dual media filters during filter run was over three times larger than that for the sand filter. The dual media filters could be operated at a high filtration rate of 360 m/day.

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여재 종류에 따른 역삼투법 해수담수화 시설 전처리 여과공정의 성능비교 (Comparison of the filtration performance by different media in pretreatment of seawater desalination by reverse osmosis)

  • 김승현;윤종섭;이석헌
    • 상하수도학회지
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    • 제23권2호
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    • pp.215-222
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    • 2009
  • This study compares the performance of the filters with various media in pretreatment of seawater desalination by reverse osmosis. For this purpose, Masan bay seawater is used as raw water. The filter performance is evaluated by the filtrate quality and the head loss development. Five media is selected in this study: anthracite, $Filtralite^{(R)}$, sand, Pumice, $AFM^{(R)}$. These media are used in combination for dual media filter and alone for mono media filter. The comparison results show that NC0.8-1.6 is the best $Filtralite^{(R)}$. The dual media filter of NC0.8-1.6 and sand outperformed other filters in particle removal. The dual media filter of anthracite and sand showed good performance in organic removal. The mono media filter of Pumice produced the similar filtrate quality as the mono media filter of sand although the effective size of Pumice is considerably greater than that of sand. Due to big size, head loss development is maintained slow in the filtration of Pumice.

급속여과공정에서의 여과보조제 사용에 따른 여과특성 (Characteristics of High-Rate Filtration with Filtration Aids)

  • 안종호;윤재흥
    • 상하수도학회지
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    • 제14권3호
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    • pp.260-270
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    • 2000
  • The objective of this study is to evaluate the effect of filter aids in the dual-media rapid filtration. Paper-filter tests were conducted to determine the proper dosages of coagulant and filter aid, and pilot plant tests using two dual-media filter columns were performed for a variety of filtration rates. Using a filter aid (non-ionic polymer), the maximum feasible filtration rate is 480m/day, while turbidity is less than 0.3 NTU and filter run-time is about 70 hours. It is possible to increase the filtration rate up to 360 m/day for keeping the turbidity less than 0.1 NTU. Turbidity increases for the filtration rate greater than 360m/day. In general, the quality of filtered water with a filter aid is stable, while the filter maintains a sufficient filter run-time for a maximum allowable head loss. Particularly, the initial breakthrough can be effectively controlled. The use of a filter aid may be one of the methods applicable if the turbidity of filtered water is required to be improved or if the filter breakthrough limits filter run-time.

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하수처리장 방류수를 이용한 인공함양 가능성 평가

  • 김병군;서인석;홍성택;김형수
    • 한국지하수토양환경학회:학술대회논문집
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    • 한국지하수토양환경학회 2002년도 추계학술발표회
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    • pp.257-260
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    • 2002
  • The main purpose of this research is to find suitable treatment methods of wastewater effluent for artificial recharge. For this purpose, we search the effluent quality of wastewater treatment plant and possibility of additional filtration process. Particles ranged 2 ~ 5 ${\mu}{\textrm}{m}$ and 15~20 ${\mu}{\textrm}{m}$ in "T" WWTP(Waste Water Treatment Plant) effluent were relatively dominant. In dual-media filtration system operation, head-loss development of column 1 was about two times faster than column 2, and head-loss development within 5 cm from surface was very important factor in operation, Conclusively, for the stable filtration and running time of 1.5~2 day, influent turbidity must keep 5 NTU or below, and filtration system must operated at 280 m/day or below. After filtration of WWTP effluent, water quality reached satisfactory level. This water has potential of agricultural reusing, flushing water in building, recharging water to river or stream at dry season and artificial recharge of ground water.und water.

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여재구성에 따른 탁질입자 제거특성 및 효율 비교 (Pilot-Scale Evaluation of Granular Filters Using Particle Distribution Analysis)

  • 안종호;윤재흥
    • 대한환경공학회지
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    • 제22권5호
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    • pp.919-926
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    • 2000
  • 정수장 여과지 모형실험장치를 이용하여 수중입자입도분석에 의한 모래 및 이중여재 여과지에 대한 여과특성 및 효율 평가를 탁도분석과 비교하여 실시하였다. 수중입자입도분석은 여과지의 효율 평가를 위한 훌륭한 평가방법으로 탁도분석에 비해 민감도가 뛰어나 여과유출수의 탁질누출 현상을 뚜렷이 관찰할 수 있었다. 모래여과지의 경우는 여과지속시간 내내 비교적 양호한 수질을 보여, 허용수두하에서는 초기탁질누출보다는 여과말기의 수위상승에 대한 주위가 필요하다. 반면에 이중여재 여과지의 경우는 내부여과에 의한 탁질의 침투가 이루어지므로 최적운영을 위해서는 적절한 여재구성과 각 여과지별로 연속적인 수질모니터링에 의한 탁질누출제어가 요구된다. 또한 보다 안정적이고 효율적인 수질의 확보를 위해서는 여과보조제의 사용도 고려되어야 할 것이다.

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