• 상하수도학회지
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• 제21권3호
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• pp.341-348
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• 2007

The efficiency of powdered activated carbon (PAC) for removing taste and odor (T&O) in drinking water supplies is dependent on the contact time, quality of mixing, and the presence of competing compounds. All of these are strongly influenced by the stage in the treatment process at which the PAC is added. In conventional water treatment plants (WTPs), PAC is commonly added into the rapid mixing basin where chemicals such as coagulants, alkaline chemicals, and chlorine, are simultaneously applied. In order to prevent interference between PAC and other water treatment chemicals, alternative locations for addition of PAC, such as at transmission pipe in the water intake tower or into a separated PAC contactor, were investigated. Whatever the location, addition of PAC apart from other water treatment chemicals was more effective for geosmin removal than simultaneous addition. Among several combinations, the sequence 'chlorine-PAC-coagulant' produced the best result with respect to geosmin removal efficiency. Consequently, when PAC has to be applied to cope with T&O problems in conventional WTPs, it is very important to prevent interference with other water treatment chemicals, such as chlorine and coagulant. Adequate contact time should also be given for adsorption of the T&O compounds onto the PAC. To satisfy these conditions, installation of a separated PAC contactor would be the superior alternative if there is space available in the WTP. If necessary, PAC could be added at transmission pipe in the water intake tower and still provide some benefit for T&O treatment.

• 한국환경과학회지
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• 제7권1호
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• pp.74-80
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• 1998

Because permeate flux was very low as It has the suspension soled of higher concentration In the trafiltration membrane separation treatment of dyestuff wastewater, pre-treatment of Ponton reaction was carried out. In the case of pH 3, COD removal rate was the hi각erst of 58%. When PAC was added into the pre-treatment supernatant, the COD removal rate was found to be 53% , and when COD was 153mg/L, the removal rate was 92.3% in the trafiltration separation. In addition, the effect of the addition of PAC on the permeate flux was also investigated. The decrease of permeate flux In the presence of PAC was higher than In the abscence of PAC, but the recovery of permeability by cleaning was better In the case of PAC system.

• 상하수도학회지
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• 제22권5호
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• pp.517-522
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• 2008

This study aims at an assessment of the effectiveness of taste & odor removal and transmembrane pressure changes in a pilot membrane plant(500m3/day) by adding PAC to MF process, and at providing a basis for applying it to the advanced water treatment process. The transmembrane pressure showed, in low turbidity of raw water, a tendency to decrease when PAC was injected at the Flux of 1, $1.5m^3/m^2{\cdot}d$, while it increased in high Flux($1.5m^3/m^2{\cdot}d$) in high turbidity of raw water. in addtion, it is shown that the fouling could be reduced more when PAC is injected together with appropriate amount of coagulant, than when PAC is solely injected. Taste & Odor-causing 2-MIB may not be detected in membrane filtered water, if the amount of PAC injection is increased in accordance with the increasing concentration of 2-MIB. Hence, PAC injection, as a pre-treatment process in MF membrane filtering, is supposed to be a suitable process for reducing fouling as well as for improvement effectiveness of taste & odor treatment.

• 한국환경보건학회지
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• 제25권3호
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• pp.1-6
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• 1999

This study was conducted to survey trihalomethane(THMs) levels in finished water of J water treatment plant and examine its reduction by powder activated carbon(PAC) treatment. Samples were collected weekly based and head-space technique was employed to determine THMs levels by G.C-ECD. THMs levels in finished waters were highest in August and showed close relationship with water temperature. All the samples satisfied the drinking water limit(100 ${\mu}$g/l) for THMs. The individual formation rates of THMs were 64.8% for CHCl$_3$, 28.4% for CHCl$_2$BR, 6.5% for CHClBr$_2$ and 0.3% for CHBr$_3$, respectively and showed little monthly difference. The reduction efficiency of THMs formation by PAC treatment was 67% during July and August. Bromine substituents were more efficiently reduced than CHCl$_3$ by PAC.

• 대한환경공학회지
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• 제27권10호
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• pp.1123-1128
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• 2005

흙냄새 혹은 곰팡이 냄새 등을 야기시키는 MIB는 남조류나 방선균등에 의해 생성되는 2차 대사산물이다. MIB는 일반적인 정수공정(응집, 침전, 여과)에 의해서는 쉽게 제거가 되지 않을 뿐만 아니라, 수돗물에 수 ng/L정도만 존재하더라도 소비자에게 심미적인 불쾌감을 유발시킬 수 있다. 일반적으로 MIB는 정확한 양의 PAC가 투입될 때 효과적으로 제거될 수 있으나, 대부분 정수장 운전자들은 PAC를 적당히 투입한 다음 처리 후 직접적인 관찰(냄새감지)에 근거하여 투입량을 조절함으로써 과잉투입 혹은 과소투입과 같은 결과를 야기하고 있는 실정이다. 이와 같은 배경을 바탕으로 본 연구에서는 $^{14}C$-radiolabled MIB을 이용한 등온흡착 및 흡착동역학 실험을 수행하여 HSDM에 필요한 물질전달계수와 표면확산계수를 결정하였다. HSDM은 실제 실험을 잘 모의하였으며, 실험 결과 또한 정확히 예측하였다. HSDM 결과에 근거하여 저자들은 Excel spreadsheet을 이용하여 최적 PAC 투입량 예측프로그램을 개발하였다. 개발된 프로그램을 실제 2개의 정수장에 적용한 결과 정수장 운전자의 경험에 의해 구해진 실제 PAC 투입량과 새롭게 개발된 프로그램에 의해 구해진 PAC 투입량 사이에 많은 차이를 보였다. 만약 정수장 운전자가 최적 PAC 투입량 예측프로그램을 이용하여 PAC 투입량을 결정한다면, 이 문제는 충분히 해결될 수 있을 것으로 판단된다.

• 자원리싸이클링
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• 제15권5호
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• pp.52-56
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• 2006

국내 알루미늄 재생업체에서 알루미늄 용해시 발생되는 알루미늄 폐드로스를 사용하여 수처리응집제로 사용되는 폴리염화알루미늄(PAC: Poly Aluminium Chloride)를 제조하였다. 알루미늄 폐드로스를 염산과 반응시켜 폐드로스 중에 잔류하는 금속알루미늄을 PAC용액으로 제조함으로써 수산화알루미늄과 염산을 원료로 사용하여 PAC를 제조하는 종래의 방법에 비해 제품의 원료비를 줄일 수 있고, 알루미늄 폐드로스를 재활용함으로써 매립 등으로 폐기시켜야 할 폐드로스의 양을 줄이는 효과가 있다.

• 상하수도학회지
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• 제10권4호
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• pp.94-102
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• 1996

This study was accomplished to get the basic data for the optimum chemical feed, evaluating interference between tastes and odors chemicals and coagulants in existing water treatment processes. During the tastes and odors occurs at D intaking tower area in 1995, PAC(Powdered Activated Carbon) feed with coagulants was PAC feed only and with coagulant simultaneously were appeared TON removal efficiency about 84%-87% within 20 min reaction time, but feed with time intervals was about 98% TON removal efficiency. Therefore in the case of PAC feed with coagulant, it is effective to feed coagulant on some time intervals in removing tastes and odors. It is not effective to feed PAC with chlorine dioxide($ClO_2$) or chlorine simultaneously in removing tastes and odors, because these chemicals were reduced the adsorption capacity of PAC.

• Membrane and Water Treatment
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• 제9권4호
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• pp.285-292
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• 2018

In the following study, Artificial Neural Network (ANN) is used for prediction of permeate flux decline during oily wastewater treatment by hybrid powdered activated carbon-microfiltration (PAC-MF) process using mullite and mullite-alumina ceramic membranes. Permeate flux is predicted as a function of time and PAC concentration. To optimize the networks performance, different transfer functions and different initial weights and biases have been tested. Totally, more than 850,000 different networks are tested for both membranes. The results showed that 10:6 and 9:20 neural networks work best for mullite and mullite-alumina ceramic membranes in PAC-MF process, respectively. These networks provide low mean squared error and high linearity between target and predicted data (high $R^2$ value). Finally, the results present that ANN provide best results ($R^2$ value equal to 0.99999) for prediction of permeation flux decline during oily wastewater treatment in PAC-MF process by ceramic membranes.

• 한국환경과학회지
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• 제8권5호
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• pp.625-631
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• 1999

This study was performed to determine the optimum coagulant dosing for effective treatment of raw water in Chinyang lake. Removal rates of algae and characteristics of the water according to coagulants dosage were investigated by treatment with Microcystis aeruginosa, which is a kind of blue-green algae, to the raw water below 5NTU. The coagulants dosage for maximum removal rate of algae were 30 mg/$\ell$ of Alum, 30 mg/$\ell$ of PAC and 10 mg/$\ell$ of PACS, respectively. The removal rate of algae in 30 mg/$\ell$ of PAC was highest as 85% compared with the other treatments. At the point of maximum removal rate of algae, the removal rates of turbidity were 34%, 66% and 22% in Alum, PAC and PACS, respectively. Residual Al was decreased depend upon decreasing turtidity in water by treatment of Alum or PAC, but decreased depend upon increasing turbidity in water by treatment of PACS. The removal rate of ${Mn}_{2+}$ in water was high in the order of Alum, PAC and PACS treatment. And ${Fe}_{2+}$ in water was not changed by treatemnt of these coagulants. Particle numbers distributions according to the particle size of suspended solids that were not precipitated at 8 min. of settling time after treatment of coagulants dosage for the maximum removal rate of algae were investigated. Most of the particle sizes were below 30 $\mu$m and particle numbers distributions below 10 $\mu$m were 64%, 56% and 66% by treatment of Alum, PAC and PACS, respectively. Zeta potential was in the range of -6.1~-9.7 mV at optimum coagulants dosage for algae removal.

• 대한환경공학회지
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• 제36권2호
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• pp.96-102
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• 2014

강화된 수질기준 이하로 인을 제거하기 위해, 혐기조, 무산소조와 Bio-clod와 다공성 폴리우레탄 여재가 충진된 접촉 산화조로 구성된 생물학적 고도처리 공정을 대상으로 PAC (Poly aluminium chloride, 10.4% as $Al_2O_3$)적용 시 인제거의 효율을 검토하였다. 접촉산화조 유출수를 대상으로 Jar-test를 실시하여 최적 PAC 주입농도를 15 mg/L로 선정 후, 2차 침전조 전단에 PAC를 주입하여 응집 침전 후 상등수를 분석하였다. PAC 주입 후 BOD와 COD의 제거율의 경우 각각 96.1%와 88.8%로, 주입 전의 95.4%와 72.4%로 효과가 크지 않았으나, TP의 제거율은 97%로 주입 전의 71.6%에 비해 18.4% 향상됨을 알 수 있었다. 특히 SP 제거율은 응집제 주입 전 59.5%에서 주입 후 98.6%로 분석되어, PAC의 적용으로 SP 제거가 가능함을 알 수 있었다. 실험기간 동안의 유출수의 TP농도는 0.13 mg/L 이하로, 추가적인 총인처리시설 설치 없이도 수질기준 준수가 가능하였다.