• 펄프종이기술
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• 제37권3호
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• pp.59-65
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• 2005

There are accumulations of remained chemical additives and contaminants in the process water of semi-closed linerboard mill. High temperature of the process water aggravates the anaerobic digestion of contaminated process water and causes the generation of hazardous gases, which are from the biological reaction of varied additives and contaminants. The hydrogen sulfide in the gases easily combine with moisture in the air, and become sulfuric acid, which causes corrosion of paper machinery. This hydrogen sulfide is from the reduction of sulfate ions in the process water, and the sulfate ions are mostly from the alum. We changed the alum to PAC (Poly Aluminum Chloride). The results were preventing generation of hydrogen sulfide, and equivalent sizing effect by the use of PAC.

• 한국물환경학회지
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• 제18권3호
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• pp.313-319
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• 2002

Laboratory experiments using metal coagulants[alum, PAC(Poly Aluminum Chloride)] and polymer were conducted in this study to enhance dewatering and settling characteristics for swine wastewater. In this study, application of mixture of metal coagulants and polymer improved settling and dewatering characteristics for swine wastewater compared to using only metal coagulants. Also sludge volume was decreased when the mixture was applied. About 80-90% of settling velocity was increased and thickening ratio was increased as much as two times when adding 100mg/L of cationic polymers. Polymer was excellent for enhancing dewatering property among coagulants.

• Korean Membrane Journal
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• 제1권1호
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• pp.100-105
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• 1999

A novel system to thicken the concentrated colloidal solution from membrane water treat-ment processes was developed. A hollow-fiber microfilter(hydrophilic polyethylene nominal pore size 0.1 ${\mu}$m total surface area 0.42 m2) was installed in an acrylic housing that has an aeration port 5 cm below the membrane and a clarifier in the bottom. The concentrate was uniformly supplied from the top of the housing. Bacuum filtration caused downward flow of concentrate and as a result thickening interface. The addition of poly-aluminum chloride (PAC) resulted in rapid increase of trans-membrane pressure (TMP) and in no improvement of the filtered water turbidity and thickening process. Two types of con-centrate and concentrate turbidity had little effect on the increase of TMP and concentrate thickening. It was observed that for the same height of membrane housing membrane surface area to housing volume (A/V) ratio had significant effect on the increase of TMP. When the housing volume was increased ten times the increasing rate of TMP was three times faster as compared to the original housing. A hydraulic model successfully simulated the formation and sedimentation of thickening interface.

• 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.

• 대한환경공학회지
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• 제36권11호
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• pp.747-752
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• 2014

인공방사성핵종 I-131은 물속에서 요오드 이온($^{131}I^-$), 요오드산염 이온($^{131}IO_3{^-}$) 등 대부분 이온상태로 존재했으며 접촉시간이 짧을 경우, 정수약품(PACl)과 분말활성탄(PAC)에 의해 제거되지 않는 것으로 나타났다. 원수 탁도 증가에 따른 I-131의 제거 효과는 없었으나 분말활성탄과 I-131과의 접촉시간 증가에 따른 I-131의 제거율은 증가하는 것을 확인하였다. 혼합 주입(PACl + PAC)에 의한 I-131을 40% 이상 제거하기 위해서는 PACl 24 mg/L 이상, PAC 40 mg/L 이상을 주입해야 하는 것을 알 수 있었다. 모래여과에 의한 I-131은 제거되지 않은 것으로 나타났으며, 입상활성탄(GAC)에 의한 제거율은 신탄, 구탄 모두에서 최소검출한계 0.10 Bq/L 미만으로 거의 100% 제거됨을 알 수 있었다. 막에 의한 I-131의 제거율은 정밀여과막에 의해서는 제거되지 않았으며 역삼투막에서는 92%가 제거되었다.

• 한국물환경학회지
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• 제28권2호
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• pp.300-304
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• 2012

It has a limitation to satisfy the phosphorus effluent criteria of 0.2 mg/L which will be reinforced from 2012 with the Biological Nutrient Removal (BNR) process. The chemical coagulation process has been operated in parallel with the biological treatment process for advanced treatment of phosphorous in the developed countries including Europe. However, the coagulation process has some disadvantages such as the desired goal may not be achieved without injecting the optimum dosage of the coagulant. This study developed the automatic control system to inject the optimum dosage of phosphorous coagulant into the coagulation process. The adopted coagulant was 10% Poly Aluminum Chloride (PAC) in this study. The automatic control system developed in this study was adopted for the treatment of the phosphorus from the effluent in SBR process. The automatic control system was composed of the data receiving part, the optimum coagulant dosage control part and the data transmit part. The result of the phosphorous advanced treatment of the SBR effluent using the automatic control system showed the removing efficiency over 95% consistently with the phosphorous concentration under 0.02 ~ 0.15 mg/L. The reproducibility analysis for checking the safety of automatic control system showed more than 95% correlation.

• 상하수도학회지
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• 제32권2호
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• pp.89-96
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• 2018

This study aimed to investigate the feasibility of improving dewaterability and settleability of sewage sludge using coagulation sludge. When mixed with sewage sludge and coagulation sludge at 1:1 ratio, capillary suction time(CST) and specific resistance to filtration(SRF) decreased by about 56% and 68%, respectively. It is found that total solids(TS) and volatile solids(VS) of mixing sludge are increased by about 59% and 53%, respectively. Also, the turbidity of the mixing sludge supernatant was reduced from 99 to 16 NTU. It is observed that the mixing of sewage sludge and coagulation sludge at 1:1 showed better effect than using poly-aluminum chloride(PAC) coagulant at 25 mg/L.

• 멤브레인
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• 제1권1호
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• pp.100-100
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• 1991

A novel system to thicken the concentrated colloidal solution from membrane water treat-ment processes was developed. A hollow-fiber microfilter(hydrophilic polyethylene nominal pore size 0.1 μm total surface area 0.42 m2) was installed in an acrylic housing that has an aeration port 5 cm below the membrane and a clarifier in the bottom. The concentrate was uniformly supplied from the top of the housing. Bacuum filtration caused downward flow of concentrate and as a result thickening interface. The addition of poly-aluminum chloride (PAC) resulted in rapid increase of trans-membrane pressure (TMP) and in no improvement of the filtered water turbidity and thickening process. Two types of con-centrate and concentrate turbidity had little effect on the increase of TMP and concentrate thickening. It was observed that for the same height of membrane housing membrane surface area to housing volume (A/V) ratio had significant effect on the increase of TMP. When the housing volume was increased ten times the increasing rate of TMP was three times faster as compared to the original housing. A hydraulic model successfully simulated the formation and sedimentation of thickening interface.

• 한국환경농학회지
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• 제18권4호
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• pp.332-338
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• 1999

전기화학적 방법에 의한 축산폐수의 효과적인 처리를 위하여 스테인레스 전극판 및 알루미늄 전극판을 이용한 회분석 실험에서는 전압, 전극판 간격 및 전해용액 주입농도별 오염물질의 처리효율을 조사한 결과는 다음과 같다. 전압별 전기화학반응 실험 결과 두가지 전극재질 모두 전압이 높을수록 전기화학반응조 내의 온도 및 pH는 상승하였으나, EC는 감소하는 경향이었다. COD 및 T-N처리율은 두가지 전극재질 모두 전압이 높을수록 전반적으로 증가하였고, SS처리율은 두가지 전극재질 모두에서 전압의 세기에 관계없이 반응초기에 약 90% 이상이었으나 20V에서는 15분 그리고 30V에서는 12분 이상 전기화학반응을 시켰을 경우에는 그 처리율이 80% 이하로 감소되었다. T-P처리율은 두가지 전극재질 모두에서 전압의 세기에 관계없이 약 90% 이상이었다. 전극판 간격별 전기반응 실험 결과 COD, T-N 및 T-P처리율은 두가지 전극재질 모두 전극판 간격이 좁을수록 대체적으로 증가하였으며, SS처리율은 두가지 전극재질 모두 전극판 간격에 관계없이 반응초기에 약 90% 이상이었다. 전해용액인 PACS의 주입농도별 전기반응 실험 결과 COD, T-N 및 T-P 처리율은 PACS의 주입농도가 증가할수록 대체적으로 증가하였으나 PACS의 주입농도가 200㎎/l 이상에서는 오염물질의 처리효율이 별 차이가 없었고, SS처리율은 두가지 전극재질 모두 약 90% 이상이었다. 이상의 회분식 실험결과 전기화학적 방법에 의한 축산폐수의 최적 처리 조건은 전압 20V, 전극판 간격 1㎝ 그리고 PACS 주입농도 200㎎/l 인 것으로 판단되었다.

• 상하수도학회지
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• 제34권6호
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• pp.463-471
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• 2020

A 1,000 ㎥/d DAF(dissolved air flotation) pilot plant was installed to evaluate the performance of the floating process using the Nakdong River. Efficiency of various DAF operations under different conditions, such as hydraulic loading rate, coagulant concentration was evaluated in the current research. The operation conditions were evaluated, based on the removal or turbidity, TOC(total organic carbon), THMFP(trihalomethane formation potential), Mn(manganese), and Al(aluminum). Also, particle size analysis of treated water by DAF was performed to examine the characteristics of particles existing in the treated water. The turbidity removal was higher than 90%, and it could be operated at 0.5 NTU or less, which is suitable for the drinking water quality standard. Turbidity, TOC, and THMFP resulted in stable water quality when replacing the coagulant from alum to PAC(poly aluminum chloride). A 100% removal of Chl-a was recorded during the summer period of the DAF operations. Mn removal was not as effective as where the removal did not satisfy the water quality standards for the majority of the operation period. Hydraulic loading of 10 m/h, and coagulant concentrations of 40 mg/L was determined to be the optimal operating conditions for turbidity and TOC removal. When the coagulant concentration increases, the Al concentration of the DAF treated water also increases, so coagulant injection control is required according to the raw water quality. Particle size distribution results indicated that particles larger than 25 ㎛ showed higher removal rates than smaller particles. The total particel count in the treated water was 2,214.7 counts/ml under the operation conditions of 10 m/h of hydraulic loading rate and coagulant concentrations of 60 mg/L.