• 상하수도학회지
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• 제25권2호
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• pp.231-240
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• 2011

The objectives of this research are to investigate coagulation efficiencies of two coagulants l.e., alum and polyaluminum chloride and to understand effects of the coagulants on membrane fouling in microfiltration. The turbidity of supernatant from alum coagulation was increased with increasing doses whereas the turbidity from PACl coagulation was maintained at the low values. The observed injection volume of PACl for the same removal was approximately 30 percent less than alum, which produced a low sludge volume. The settling velocity of PACl flocs was greater than alum flocs. The results corresponded well with floc size measurements. Flux decline from alum coagulation was significant due in part to small sizes of flocs. At the low dose, alum floc had less specific cake resistance than PACl floc. However, as the dosage was increased, the increases in specific cake resistances of alum was substantial. Alum coagulation pretreatment needs careful operation to reduce membrane fouling by flocs. In general, PACl coagulants were more effective than alum coagulants for pretreatment of membrane processes because PACl showed the better performance in coagulation and membrane fouling.

• 한국환경보건학회지
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• 제27권3호
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• pp.43-48
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• 2001

Terephthalic acid and ethylene glycol resulting form the weight-reduction process of polyester make trouble in the operation of activated sludge process. Also, polyester weight loss wastewater shows high pH, high organic strength and wide variation of organic loading. Therefore, this study was conducted in order to improve treatment efficiency by activated sludge process with Pseudomonas sp degrading components of polyester weight loss wastewater. The CO $D_{Mn}$ and BO $S_{5}$ of the waste wastewater were 560~3,000 mg/$\ell$ and 8000~3,000 mg/$\ell$, respectively. pH was 11.8~12.3. COD removal efficiency by activated sludge-coagulation process with Pseudomonas sp was 94.1~95.8% for 35 hr of hydraulic retention time. Total organic carbon removal efficiency was 97.1%. Ethylene glycol and terephthalic acid in the wastewater were completely degraded during 32 hr of hydraulic retention time.e.

• 한국막학회:학술대회논문집
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• 한국막학회 1999년도 Energy Saving Membrane Separtion Systems 에너지 절약형 막분리 시스템
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• pp.39-39
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• 1999

Membrane separation technology has become a more attractive technology on waste water treatment and water recycle in recent years. On this application, membrane does not take main part of treatment, such as decomposition or handling of organic matter in the waste water, but it is very important supporting method in the total system. Activated sludge is most popular method as main part. In the system , membrane works as a separator to obtain clear water after biological treatment, by which the permeate could be released, recycled or applied to further additional treatment, instead of conventional sedimentation, coagulation and sand filtration. We would like to introduce our system cases for waste water treatment and water recycle, in which membrane separation technology works. In most of cases, membranes are applied to solid- liquid separation of activated sludge. Our experiences will be introduced as following items.

• 한국산업융합학회 논문집
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• 제16권2호
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• pp.35-39
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• 2013

This paper synthesized the new copper removal agent(PW-2001) and investigated removal efficiency of copper, COD, calcium, SS and sludge amounts. Removal efficiency of copper were 96.1% and 99.1% with the lime and PW-2001, respectively while COD removals reached up to 38% and 69.6% with the use of lime and PW-2001. The concentrations of calcium and SS with PW-2001 were decreased 2.68 and 4.95 times lower than those with lime. Amount of sludge with PW-2001 was 60% smaller than lime. Quantity of PW-2001 needed for coagulation only reached 58.7, compared to lime standard quantity(100), and total cost of copper removal with PW-2001 was saved 25% more than lime.

• Journal of Advanced Marine Engineering and Technology
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• 제33권8호
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• pp.1187-1195
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• 2009

본 논문은 완전 혼화조를 이용한 폐수처리 공정의 응집특성에 대한 연구를 목적으로 한다. 완전 혼화조 시스템은 유체 저장조, 임펠러가 장착된 3단의 혼화 및 응집부, 응집보조제 및 응집제 주입부, 응집 침전조 그리고 제어부로 구성된다. 실험용 폐수는 터널 공사현장에서 폐수 슬러지를 수거하여 약 1,000NTU의 탁도를 갖도록 만들었다. 응집보조제의 주입량이 증가함에 따라 약 99% 정도까지 탁도 제거율이 증가하였으며, 응집제의 주입량이 일정한 범위 이상으로 증가하면 탁도 제거율이 감소하는 것을 알 수 있다.

• 공업화학
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• 제20권1호
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• pp.34-39
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• 2009

본 연구는 염색폐수 처리공정에서 발생하는 슬러지 및 색도제거에 관한 연구로 응집제가 색도제거에 미치는 영향에 대한 상관성을 규명하는데 목적이 있다. 이를 위해 실제공정에서 배출되는 염색폐수를 대상으로 응집조건에 따른 특성을 분석하였다. 응집제로 $FeCl_3$, $FeSO_4$, $Al_2(SO_4)_3$를 사용하였으며, 실험에 사용된 염색폐수의 BOD, COD, pH, 그리고 색도의 평균값은 각각 800 mg/L, 600 mg/L, 9.7, 182 이었다. 실험결과에 의하면 응집제의 농도가 335~2000 mg/L 이고 NaOH의 농도가 500 mg/L인 조건에서 응집제로 $FeCl_3$를 사용하였을 때 색도제거효과가 가장 우수하였다. 색도제거효과는 폐수의 pH와 응집제의 농도에 따라 결정된다고 할 수 있다.

• 공업화학
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• 제10권7호
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• pp.1073-1078
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• 1999

본 연구의 목적은 소오다회 제조 공장에서 발생하는 폐슬러리를 미세 실리카가 함유된 공장 폐수의 응집제로 이용 가능한 지를 확인하고 이로부터 폐수 처리비용을 절감하고자 수행되었다. 실리카 함유 폐수를 처리하는 경우 단순히 응집 처리하는 기존의 방법과는 달리 수중에 미립자로 존재하는 실리카를 먼저 겔화(gellation)시킨 후 응집 처리하는 방법을 사용한 경우, 적은 양의 폐슬러리를 사용하여도 양호한 처리수질을 얻을 수 있어 소오다회 폐슬러리를 실리카 함유 폐수 처리를 위한 응집제로 재이용이 가능함을 확인할 수 있다. 폐수 중 실리카의 겔화를 위한 적정 pH는 5정도였으며 겔화에 의한 응집 처리시 약품 사용량의 감소와 응집 수 발생되는 슬러지 양을 감소시킬 수 있었다. 소오다회 폐슬러리로 응집시킨 플럭의 탈수성과 침강성 역시 양호한 결과를 얻을 수 있었다.

• 한국염색가공학회지
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• 제14권2호
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• pp.40-50
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• 2002

In order to remove the pollutants effectively in the dye wastewater by chemical precipitation process, coagulation arid flocculation test were carried out using several coagulants on various reaction conditions. It was found that the Ferrous sulfate was the most effective coagulant for the removal of disperse dye(B79), and we could get the best result lot the removal of disperse dye(B56) in the aspects of TOC removal efficiency and sludge field. When the Ferrous sulfate dosage was $800mg/\ell$, the sludge settling velocity was very fast>, and the color was effectively removed in the disperse dye(B79) solution. Although the color removal was ineffective when the Alum was used as a coagulant, the sludge field was decreased in comparison with the Ferrous sulfate or the Ferric sulfate was used in the disperse dye(B56) solution. The general color removal effect for the disperse dye(B56 and B79) solutions, the Ferric sulfate was more proper coagulant than the Alum. It was showed that TOC removal was improved 5% and over by the addition of Calcium hydroxide, and $30mg/\ell$ of sludge yield was decreased(B79). When Alum or Ferric sulfate was used as a coagulant, pH condition for most effective color removal was 5 in B56 solution. In case of Ferrous sulfate as a coagulant, most effective pH condition for color removal was 9. When Ferric sulfate or Ferrous sulfate was used as a coagulant, pH condition for most effective color removal was 9 in B79 solution.

• 상하수도학회지
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• 제24권5호
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• pp.527-536
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• 2010

Although the bubble-floc agglomerate floated and formed the float layer on the surface of the water in the DAF process, after inducing in the thickening tank a part of the bubble-floc agglomerate come up again to the surface and the other is settled at the bottom of the tank. The bubble-floc agglomerate divided into two group as the scum on the surface and the sludge of the bottom gives rise to operational troubles for the thickening process. In order to find out the cause of break-up and the effective thickening method for sludge from the DAF process, the composition of the bubble-floc agglomerate was investigated and a series of flotation experiments carried out. There was no difference of composition between the scum on the surface and the sludge of the bottom in the thickening tank. The coagulation was not effective to improve the trouble that the bubble-floc agglomerate divided into the scum and the sludge. It was estimated that for the bubble-floc agglomerate of thickening tank the trouble was caused by not the change or the difference of chemical composition but whether the bubble-floc agglomerate hold bubbles. Furthermore, for the effective thickening of sludge from the DAF process, it is required an additional flotation applied the AS ratio depending upon the solid concentration of sludge as the operation parameter.

• Environmental Engineering Research
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• 제20권4호
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• pp.392-396
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• 2015

This work aims to investigate the oily wastewater treatment by the electrocoagulation-flotation (ECF) and propose a mathematical model for the efficiency prediction. Cutting oil was used to prepare the synthetic oily wastewater with submicron droplet sizes. The chemical coagulation by aluminium sulfate was firstly tested following by the electrocoagulation-flotation with aluminium electrodes. Both processes gave the effective treatment performance with the efficiencies higher than 90%. However, the ECF consumed less aluminium dosage as well as produced less sludge, which were its advantage on the chemical coagulation. The performance of the ECF was found to be affected by the current density, oil concentration, and reaction time according to the analysis by the design of experiment (DOE). Finally, the prediction model was proposed by two approaches, including linear and logarithm function. The latter model gave more accuracy prediction results in terms of treatment efficiency and duration in the lag and stable stages.