• 한국염색가공학회지
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• 제9권6호
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• pp.26-32
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• 1997

In order to remove the pollutants effectively in the dye-processing wastewater by chemical precipitation, coagulation and flocculation test was carried out using several coagulants on various reaction conditions. It was found that the Ferric sulfate was best coagulant for the treatment of mixed dye-processing wastewater. When the Ferric sulfate dosage was 1,100mg/$\ell$, the COD removal rate was very high(50%), and the color was removed very effectively. The COD was decreased relatively well up to 40%, when Alum was dosed as coagulant. But it was difficult to remove the color effectively. Test results about COD removal for the Ferrous sulfate and the Ferric chloride used were mostly same as those of the Alum used. However, the color removal by the Ferrous sulfate was much better than the case of the Alum or the Ferric chloride. It was found that the COD removal was increased and the sludge yield was decreased by pH control before polymer flocculant addition, during the jar test for the Ferrous sulfate and the Ferric sulfate as a coagulant.

• 상하수도학회지
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• 제9권3호
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• pp.99-107
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• 1995

Various humic substances are widely distributed in natural water body, such as rivers and lakes and cause the yellowish or brownish color to water. The evidence that humic substances are precursors of THMs formation in chlorinated drinking water has been reported m the Jiteratures. For the reason of public health as well as aesthetics, needs for humic substances removal have been increased in the conventional water treatment processes. In this research, the characteristics of aluminium coagulation of humic acids and humic acids were investigated. The optimum pH and coagulants dosage to remove these materials simultaneously by coagulation were alto studied. The results are as followed; 1. UV-254 absorptiometry for measuring the concentration of aquatic humic acids showed good applicability and stable results. 2. The optimal pH range for humic acids removal by aluminium coagulation was 5 to 5.5, however, an increase in aluminium coagulant dosage could enhance the removal rate of humic acids in the wide pH range. 3. Coprecipitation of humic acids in the typical pH range of 6.5 to 8 in water treatment processes may require the sweep coagulation mechanism with the excess aluminium coagulant dosage. 4. Using PAC(poly aluminium chloride) or PASS(poly aluminium silica sulfate) as coagulants was able to expand the operating range for removing humic acids. 5. From the coagulation of humic substances(UV-254) and turbidity at pH range of 5.5 - 6.0 and alum dose of 86 ppm, the removal efficiency of turbidity from the reservoir water was above 90% and that of UV-254 was above 70%. 6. By using the reservoir water, the optimum condition of rapid mixing for simultaneous removal of turbidity and UV-254 absorbance was pH of 5.8 and LAS dose of 86 ppm, in this study.

• 멤브레인
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• 제22권2호
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• pp.135-141
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• 2012

본 연구는 Y 정수장의 세라믹 정밀여과막 공정을 위한 최적의 응집 조건을 도출하고자 수행되었다. 쟈테스트 결과 Y댐 원수의 pH를 7로 조정 시 응집효율이 가장 우수하였으며, 원수 탁도가 10 NTU 이하인 평상시 탁도 조건하에서 최적 응집제 주입량은 3 mg/L (as $Al_2O_3$)인 것으로 나타났다. 최적 응집제를 선정하기 위하여 응집제 종류(PAC, PACS (II), PAHCS)별로 미니모듈 실험장치를 이용하여 평가한 결과 PAC를 주입하고 원수 pH를 7로 조정한 경우 비여과유속 감소율이 가장 낮은 것으로 나타났다. 원수 탁도를 10~150 NTU로 변화시키며 미니모듈에서 비여과유속 감소율을 평가한 결과 원수탁도 10~30 NTU 조건에서는 응집제 주입량 증가에 따라 비여과유속 감소율이 크게 감소하였으나 원수탁도가 50 NTU 이상에서는 응집제 주입량을 증가시켜도 비여과유속 감소율에 큰 차이가 없는 것으로 나타났다. 따라서 Y 정수장을 위해서 는 원수탁도 10 NTU 이하에서는 PAC (11% as $Al_2O_3$) 30 mg/L, 10~50 NTU에서는 30~50 mg/L, 50 NTU 이상에서는 50 mg/L이 적절하다.

• 한국환경과학회지
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• 제12권3호
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• pp.281-286
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• 2003

This study was conducted to evaluate the feasibility of ammonia removal by zeolite adsorption in drinking water treatment. In generally, drinking water treatment process is conducted coagulation/flocculation, sedimentation, sand filtration and disinfection. We tested feasibility with two method, one is powdered zeolite dosing to coagulation tank and the other is to substitute granular zeolite for sand of sand filter. In powdered zeolite test, raw water is used tap water with putting of 2 mg/l of NH$_4$$\^$+/-N. Filtration of granular zeolite was conducted with 80 cm of effective column high and 120 m/d of flow rate. At above 100 mg/1 of zeolite dosage, ammonia concentration was decreased below 0.5 mg/l of NH$_4$$\^$+/-N in powdered zeolite test. But, turbidity was increased to 30 NTU by powdered zeolite dosage. That turbidity was scarcely decreased in generally coagulant using condition in drinking water treatment. In granular zeolite test, ammonia was not detected in treated water until 8 days. This result suggest that using of granular zeolite in sand filter could be removal ammonia in winter. But we need regeneration at zeolite filtration for ammonia removal. So, it is to make clear that zeolite regeneration ability was compared KCl with NaCl. The result reveal that KCl was more excellent than NaCl. Optimum regeneration concentration of KCl was revealed 100 mM. Regeneration efficient was not increased at pH range 10∼12.5.

• 한국물환경학회지
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• 제30권6호
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• pp.653-657
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• 2014

Effects of $H_2O_2$ addition for fenton oxidation on iron coagulation for treatment of phosphorus species, such as orthophosphate, metaphosphate, pyrophosphate, organic phosphate, were investigated. The effects of coagulant dosage, hydrogen peroxide dosage and the combined sequence ferric coagulation and $H_2O_2$ addition for fenton oxidation and coagulation were studied. The characteristics of floc growth rate were monitored using the PDA. The removal efficiencies of phosphorus species by iron coagulation were increased as Fe/P molar ratio increased. However, the removal efficiencies of metaphosphate, pyrophosphate, organic phosphate by a ferric coagulation were not increased as Fe/P molar ratio increased. The removal efficiency of metaphosphate, pyrophosphate, organic phosphate was increased by using iron coagulation and $H_2O_2$ addition for fenton oxidation. The result indicated that non-reactive phosphorus after iron coagulation was changed to reactive phosphorus by $H_2O_2$ addition for fenton oxidation and the oxidized iron enhanced the coagulation efficiencies.

• 상하수도학회지
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• 제23권4호
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• pp.459-469
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• 2009

It is well known that coagulation pretreatment can reduce foulants prior to membrane filtration. The purpose of this research was to investigate the effects of coagulation on fouling of ceramic microfiltration membrane($0.1 {\mu}m$) using pilot plant of $150m^3/day/train$ capacity. Train A membrane system has pretreatment process of ozonation and coagulation while train B has only coagulation. Two types of coagulation operation were investigated: back mixer(rapid mixing with or without slow mixing) which is a conventional mechanically stirred mixer and an inline static mixer. Ozone dose rate for train A was 1 mg/L and ozone contact time was 12 min. The coagulation dose(PACl 10% as $Al_2O_3$) rate was changed 20~40 mg/L according to experimental schedule. In this experimental conditions, the coagulation of back mixer type with rapid mixing(GT=72,000) and slow mixing(GT=45,000) was the best effective in reduction of ceramic membrane fouling regardless preozonation. Especially, the effect of inline static mixer was sensitive to change in water quality. Ozonation mainly affected irreversible fouling rather than reversible fouling in accordance with less adsorption of NOM on the membrane surface. Thus, the increase rate of the nomalized TMP(trans membrane pressure) at $25^{\circ}C$ for train A was relatively lower than that of train B under same coagulation process with same coagulant dosage. The best performance of ceramic membrane appeared in case of combined process with ozonation, therefore this integrated process is able to archive less coagulant dosing and secure a stability of ceramic membrane system.

• 대한환경공학회지
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• 제30권1호
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• pp.85-89
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• 2008

정수 처리공정의 응집 침전공정에서 무기고분자응집제를 이용한 미세조류의 제거 가능성을 파악하기 위해서 응집제의 종류(Alum, PAC)와 응집영향인자(알칼리도, 응집제 주입량, 침전시간)에 따른 미세조류의 제거율과 미세조류의 크기(micro-, nano-, picoplankton)별 제거율과 주입된 응집제가 미세조류의 제거에 미치는 기여율을 평가하였다. 알칼리도의 주입량에 따른 조류의 제거율은 Alum의 경우 알칼리도가 25 mg/L의 조건에서 87.2%, PAC의 경우 알칼리도가 30 mg/L의 조건에서 90.1%로 가장 높은 제거율을 나타내었다. 조류의 제거율이 가장 높은 응집제 주입량은 Alum의 경우 40 mg/L로 제거율이 88.1%이었고, PAC의 경우는 주입량이 50 mg/L에서 제거율이 89.0%로 가장 높은 제거율을 나타내었다. 그리고 조류의 제거에는 PAC보다는 Alum이 다소 유리하다는 것을 알 수 있었다. 응집제가 주입되었을 경우 주입되지 않은 조건에 비해서 조류의 제거율이 약 2배 정도 증가하는 것을 알 수 있었다. 최적조건 하에서 조류의 제거율은 nanoplankton > microplankton > picoplankton의 순으로 나타났으며, 특히 picoplankton의 제거율은 약 30% 미만으로 제거율이 매우 낮은 것을 알 수 있었다.

• 상하수도학회지
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• 제20권1호
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• pp.138-146
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• 2006

The characteristics of backwash and concentrate discharges depend upon the quality of the water being treated and the net recovery of the membrane system. This paper is to indicate a design methods on the capacities of residuals treatment facilities in membrane processes for drinking water. We operated a demonstration membrane plant with a recovery rate of 90% for designing G-water treatment plant. We investigated on design parameter (optimum coagulant dosage and surface loading rate etc.) to design efficiently the residuals treatment facilities. The settling test was conducted with 1m columns dosing PACl to kaolin and membrane residuals under the experimental condition that discharge permit was under a 60mg/L. When the quantity of membrane residuals was $1,575m^3/day$, the estimated results for 1st thickener demonstrated the surface loading rate of 14.4m/day, detention time of 5.83hr, available depth of 3.5m.

• 멤브레인
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• 제23권1호
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• pp.12-23
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• 2013

섬진강 수계의 복류수를 대상으로 막여과 정수처리 공정 현장 적용성 평가를 위해 여과막의 공경에 따른 막오염도 예측 및 최적 응집제 주입농도 선정을 통해 파일롯플랜트 규모의 검증실험을 실시하였다. 막공경에 따른 막오염도 평가를 위한 여과저항 평가실험 결과, $0.1{\mu}m$와 $0.01{\mu}m$ 여과막의 비가역적 여과저항 증가율은 각각 $0.44{\times}10^{12}/m^2$, $0.42{\times}10^{12}/m^2$로 나타났으며, Flux-test 실험결과, 적정응집제 주입농도는 Jar-Test 실험결과에 비해 낮게 나타났다. 현장 적용성 평가를 위해 6개월 동안의 파일롯플랜트 운영을 수행하였다. 응집을 실시하지 않은 막여과공정은 여과유속 $1.0{\sim}1.5m^3/m^2{\cdot}day$, 응집을 실시한 막여과 공정은 여과유속 $1.0{\sim}2.0m^3/m^2{\cdot}day$의 조건에서 운전한 결과 두 조건 모두 6개월 이상 막차압이 안정되게 유지되었다. 따라서 섬진강 수계의 복류수를 이용한 막여과 공정 운영에 있어 적정 여과유속으로 운전 시 응집제 사용 없이 안정적인 운전이 가능함을 알 수 있었다.

• 유기물자원화
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• 제14권1호
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• pp.151-159
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• 2006

런던협약의 영향으로 슬러지 처리의 중요성이 대두되고 있는 실정이므로 본 연구는 슬러지 처리에 대한 개선방안의 제시를 목적으로 유기성 폐수 및 하수처리장 슬러지를 대상으로 JAR test 및 교반장치를 부착한 침강 column을 이용하여 응집효율이 침강특성에 미치는 영향에 대한 실험을 실시하였으며 다음과 같은 결과를 얻었다. 최적의 침강효율을 얻기 위한 최소의 응집제 투여농도는 200mg/L의 경우로 나타났으며. 200mg/L 이상으로 PAC가 투여될 경우 각각의 임계슬러지 영역의 크기에서는 큰 변화가 없는 것으로 나타났다. 따라서 200mg/L로 투여되었을 때의 Clarification Rate(CR)은 임계슬러지 침강높이 비율이 0.4로 나타났으므로 CR = (Ho-Ht) / Ho = 1-0.4=0.6 로 산정되었다. MLSS농도가 높아질수록 슬러지 계면 침강속도는 감소하였으나 MLSS농도가 1,000mg/l 이상으로 증가하면 오히려 침강속도는 증가하는 것으로 나타났다. 이는 슬러지 농도가 1,000mg/l 이상으로 증가하게 되면 압밀침전영역으로 전이되어 상호작용에 의한 응집에 영향을 미치게 됨으로써 오히려 floc 형성에 긍정적인 영향을 미치기 때문이다. 슬러지 응집계면의 침강속도는 유기폐수 활성슬러지의 평균 침강속도 $4.25{\times}10^{-3}/min$보다 하수처리장 슬러지의 평균 침강속도가 $28.66{\times}10^{-3}/min$로 6.7배 높은 것으로 나타났다. 유기성 폐수 활성슬러지는 PAC의 투여량이 200mg/l 이하일 때는 침강속도 증가율보다 CR의 증가율이 더 컸으나 200mg/l 이상일 때는 CR의 증가율보다 침강속도 증가율이 더 커졌음을 알 수 있었다. 그러나 하수슬러지의 경우는 PAC 투여량이 증가함에 따라 CR의 변화율에는 차이가 적었으나 침강속도는 200m/l 이상일 때 차이가 급격히 증가하였다. 따라서 응집제 투여효과는 상등수의 SS제거율 효과보다는 MLSS의 침강속도에 더 큰 영향을 미치는 것을 알 수 있다.