• 제목/요약/키워드: coagulant dosage

검색결과 131건 처리시간 0.021초

MBR반응기의 막오염방지를 위한 활성탄과 응집제를 이용한 전처리에 관한 연구 (Using Coagulant and Activated Carbon as Pretreatment for Membrane Fouling Control in MBR (Membrane Bioreactor))

  • 김동하
    • 상하수도학회지
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    • 제20권1호
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    • pp.122-127
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    • 2006
  • The aim of this study was to investigate the characteristics of membrane fouling caused by soluble organic materials in a membrane bioreactor process. For the removal of filterable organic materials (FOC) smaller than $1{\mu}m$, coagulants and activated carbon were added. A membrane bioreactor using a submerged $17{\mu}m$ metal sieve was operated in laboratory scale to examine the possibility of membrane fouling control. As the dosage of GAC and coagulant increased, the residual FOC concentration decreased and the permeate flow rate increased markedly. The permeate flux increased with an increased PACl addition at the range from 0 to 50 mg/l. At coagulant dosage of 27mg/l, the removal of FOC was about 46% and the flux increased to 3.5 times compared to the case without PACl addition. The permeate flux increased gradually with an increase in GAC dosage. At GAC dosage of 50mg/L, the permeate flux was about 2 times higher compared that for raw water. The particle in the range of $0.1{\sim}1.0{\mu}m$ were removed effectively by the addition of GAC and coagulant. Higher osage of GAC and coagulant, led to higher removal of FOC. A different set of experiments was also performed to investigate the effect of pretreatment on the permeation ability of MBR system using the metal sieve membrane. After 40 hours of operation, the permeate flux was about 1,000 ($L/m^2-hr$), which is 20 times higher compared to the results in literature. It is likely that combined pretreatment using coagulant and activated carbon was the most effective to resolve membrane fouling problems. Moreover, the continuous operations could be successful by applying this pretreatment method.

하수처리시설에서 인 고도처리를 위한 자동제어시스템 개발에 관한 연구 (Development of the Automatic Control System for the Advanced Phosphorus Treatment in Sewage Treatment Plant)

  • 김선국;이호식;전태성
    • 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.

진양호소수의 효과적인 정수처리를 위한 최적응집제 주입량 결정 -조류제거를 위한 응집제 주입효과- (Determination of Optimum Coagulant Dosage for Effective Water Treatement of Chyinyang Lake - The Effect of Coagulant Dosing on Removal of Algae-)

  • 이원규;조주식;이홍재;임영성;허종수
    • 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.

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반응표면분석법-중심합성계획을 이용한 최적 응집제 주입량 산정 연구 (Optimization of coagulant dosage using response surface methodology with central composite design)

  • 김예슬;오재일
    • 상하수도학회지
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    • 제29권2호
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    • pp.193-202
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    • 2015
  • The determining the appropriate dosage of coagulant is very important, because dosage of coagulant in the coagulation process for wastewater affects removing the amount of pollutants, cost, and producing sludge amount. Accordingly, in this study, in order to determine the optimal PAC dosage in the coagulation process, CCD (Central composite design) was used to proceed experimental design, and the quadratic regression models were constructed between independent variables (pH, influent turbidity, PAC dosage) and each response variable (Total coliform, E.coli, PSD (Particle size distribution) (< $10{\mu}m$), TP, $PO_4$-P, and $COD_{cr}$) by the RSM (Response surface methodology). Also, Considering the various response variables, the optimum PAC dosage and range were derived. As a result, in order to maximize the removal rate of total coliform and E.coli, the values of independent variables are the pH 6-7, the influent turbidity 100-200 NTU, and the PAC dosage 0.07-0.09 ml/L. For maximizing the removal rate of TP, $PO_4$-P, $COD_{cr}$, and PSD(< $10{\mu}m$), it is required for the pH 9, the influent turbidity 200-250 NTU, and the PAC dosage 0.05-0.065 ml/L. In the case of multiple independent variables, when the desirable removal rate for total coliform, E.coli, TP, and $PO_4$-P is 90-100 % and that for $COD_{cr}$ and PSD(< $10{\mu}m$) is 50-100 %, the required PAC dosage is 0.05-0.07 ml/L in the pH 9 and influent turbidity 200-250 NTU. Thus, if the influent turbidity is high, adjusting pH is more effective way in terms of cost since a small amount of PAC dosage is required.

응집과 균질화가 팽화슬러지의 용존공기부상과 침전에 미치는 영향 (Effect of Coagulation and Homogenization on the Dissolved Air Flotation and Sedimentation of Bulking Sludge)

  • 김동석;박영식
    • 한국환경보건학회지
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    • 제33권1호
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    • pp.68-74
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    • 2007
  • The objective of this study is to examine the effect of the coagulation and homogenization in bulking sludge thickening of paper manufacturing plant using DAF(Dissolved Air Flotation) and gravitational sedimentation. The effects of parameters such as dosage of coagulant and homogenization time were examined. The results showed that DAF and sedimentation was affected aluminum sulfate and anion polymer coagulant differently. At the optimum dosage of aluminum sulfate, thickening efficiency of DAF and sedimentation process were increase 1.25 time and 2.02 time, respectively. At the optimum dosage of anion polymer coagulant, thickening efficiency of DAF process was increase 1.35 time, but thickening efficiency at sedimentation was 1.06 time. When anion polymer coagulant of 0.5 mg/l was added in DAF process, water content of sludge was decreased from 96.6% to 90.7% in dewatering process using Buchner funnel test device. After homogenization(20500 rpm, 10 min), Sauter mean diameter of sludge floc was decreased from 631 ${\mu}m$ to 427 ${\mu}m$, however increase of flotation efficiency by DAF was only 1.09 time.

폴리염화알루미늄 과량주입에 의한 고(高) pH 원수의 수처리효율 개선 (Improvement of Water Treatment Efficiency by Poly Aluminum Chloride Overdosing in High pH Raw Water)

  • 임재철;김진근
    • 상하수도학회지
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    • 제23권1호
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    • pp.39-46
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    • 2009
  • A method to improve water treatment efficiency by coagulant overdosing for high pH raw water at a drinking water treatment plant (WTP) which had no pH adjusting facilities was investigated. Poly aluminum chloride (PACl) was used for coagulant, and turbidity removal efficiency was evaluated as a function of PACl dosage increases. pH and turbidity of supernatant of jar-tester were 7.10 and 0.50 NTU respectively, when the turbidity, pH, alkalinity, water temperature, conductivity of raw water were 1.75 NTU, 9.38, 46.5 mg/L, $6.4^{\circ}C$, $400{\mu}s/cm$, respectively. Turbidity of settled water was reduced from 2.18 NTU to 0.28 NTU (87% reduction) when PACl dosage was increased from 16 mg/L to 45 mg/L at a full scale WTP. This can be attributed to the recovery of coagulant efficiency by pH reduction with the increase of coagulant dose, however coagulation efficiency was reduced with the formation of Al(OH)4- by PACl addition at higher pH. Coagulant overdosing was proven to be a rapid and effective method for high pH raw water, which can be applied at drinking WTP.

수중 Humic Acid의 효율적 응집처리와 잔류알루미늄 감소방안에 관한 연구 (A Study on the Coagulation of Aquatic Humic Acid and Reducing Residual Aluminum)

  • 김수연;정문호;두옥주
    • 한국환경보건학회지
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    • 제24권2호
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    • pp.38-46
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    • 1998
  • The purpose of this study is to evaluate and compare the effective coagulation of commercial humic acid which is well known as major precursor of trihalomethane, with LAS and PAC and to quantify the residual aluminum in the treated water. Then the optimum pH, the dosage of coagulant were determined. 1. Humic acid concentrati6n, UV absorbance and color were well correlated and UV absorbance(254 nm) and color seem to be used in quntificative analysis of humic acid of same kind. 2. Optimal dosage of LAS and PAC increase as humic acid concentration increases. And optimal pH range for coagulation using LAS is pH 5.5-7.0 and pH 3.5-6.5 for PAC. Within these ranges the removal efficiency is 90-99%. 3. The results of quantification of residual aluminum in treated water shows that minimal aluminum remains on the optimal coagulation condition. But the residual aluminum increses as the dosage of coagulant is beyond the optimal range. Thus the dosage of coagulant should be chosen with the condition on which humic acid removal is maximum and the residual aluminum concentration is minimum. 4. In the water treatment process the raw water pH range is 6.5-8.0, and it seems to be possible to remove humic acid by charge neutralization not by sweep floc. But it should be considered that different commercial humic acids have different physical and chemical characteristics.

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신경회로망을 이용한 상수처리시스템의 응집제 주입공정 최적화 (Optimization of coagulant dosing process in water purification system using neural network)

  • 남의석;박종진;장석호;차상엽;우광방;이봉국;한태환;고택범
    • 제어로봇시스템학회논문지
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    • 제3권6호
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    • pp.644-651
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    • 1997
  • In the water purification plant, chemicals are injected for quick purification of raw water. It is clear that the amount of chemicals intrinsically depends on water quality such as turbidity, temperature, pH and alkalinity. However, the process of chemical reaction to improve water quality (e.g., turbidity) by chemicals is not yet fully clarified nor quantified. The feedback signal in the process of coagulant dosage, which should be measured (through the sensor of the plant) to compute the appropriate amount of chemicals, is also not available. Most traditional methods focus on judging the conditions of purifying reaction and determine the amounts of chemicals through manual operation of field experts using Jar-test data. In this paper, a systematic control strategy is proposed to derive the optimum dosage of coagulant, PAC(Polymerized Aluminium Chloride), using Jar-test results. A neural network model is developed for coagulant dosing and purifying process by means of six input variables (turbidity, temperature, pH, alkalinity of raw water, PAC feed rate, turbidity in flocculation) and one output variable, while considering the relationships to the reaction of coagulation and flocculation. The model is utilized to derive the optimum coagulant dosage (in the sense of minimizing turbidity of water in flocculator). The ability of the proposed control scheme validated through the field test has proved to be of considerable practical value.

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진양호소수의 효과적인 정수처리를 위한 최적응집제 주입량 결정 -콜로이드성 오염물질 처리를 위한 응집제 주입효과- (Determination of Optimun Coagulant Dosage for Effective Water Treatment of Chinyang Lake -The Effect of Coagulant Dosing on Remoaval of Colloidal Pollutants-)

  • 이원규;조주식;이홍재;허종수
    • 한국환경과학회지
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    • 제7권6호
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    • pp.761-772
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    • 1998
  • 상수원수의 효과적인 처리를 위한 최적 응집제 주입량을 결정하기 위하여 상수원수의 콜로이드성 오염물질 처리를 위한 Alum, PAC 및 PACS의 응집제 주입량별 탁도제거 및 원수특성변화를 조사한 결과는 다음과 같다. 최저 잔류탁도를 나타내는 최적 응집제 주입량은 원수의 탁도가 5NTU인 경우 Alum은 35mg/ι, PAC은 30mg/ι 및 PACS는 10mg/ι이었고, 원수의 탁도가 10NTU인 경우 Alum은 30mg/ι, PAC은 25mg/ι 및 PACS는 10mg/ι이었으며, 이때 침전시간 4분 및 8분대의 탁도제거율은 원수탁도 5NTU인 경우 Alum은 10 및 72%, PAC은 44 및 62%, PACS는 25 및 55%였고, 원수탁도 10NTU인 경우에는 Alum은 52 및 70%, PAC는 90 및 95%, PACS은 10 및 28%였다. PAC이 Alum 및 PACS에 비하여 floc형성속도와 침강성이 우수하고 탁도제거율도 높게 나타나 침전지내급수량 변동이 심하고 표면부하율이 과부하일 경우 PAC을 사용하는 것이 유리할 것으로 판단되었다. 원수의 탁도별 응집제 주입량에 따른 pH 및 알칼리도는 응집제 주입량이 증가할수록 감소되었으나 각 응집제 최대 주입량에서 pH는 음용수 수질기준인 pH 5.8이하로는 감소되지 않았으며, 알칼리도도 재탁현상이 일어날 수 있는 10mg/ι 이하로는 감소되지 않았다. 처리수준 잔류 Al은 원수탁도 5 및 10NTU인 경우 Alum과 PAC은 그 주입량이 저농도에서 고농도로 갈수록 잔류탁도가 감소함으로써 잔류 Al도 감소하였으나 PACS는 잔류탁도가 증가하는 주입량에서도 잔류 Al은 감소하였다. 수중 KMnO$_4$ 소비량은 응집제 주입량이 증가할수록 감소되었으며, 최저 잔류 탁도를 나타내는 최적 응집제 주입량에서의 KMnO$_4$ 소비량 감소율은 원수탁도 5NTU일 경우 PAC 39%, Alum 18% 및 PACS 11%였으며, 10NTU일 경우에는 PAC 42%, Alum 27% 및 PACS 36%로서 전반적으로 탁도제거율과 KMnO$_4$소비량간에는 일정한 경향이 없는 것으로 나타났다. 수중 TOC는 응집제 주입량이 증가함에 따라 약간씩 감소되었으나 응집제 주입량 30mg/ι 이후부터는 일정 수준으로 유지되었으며, 감소되는 정도는 PACS >PAC >Alum순이었다. 최저 잔류탁도를 나타내는 최적 응집제 주입량에서의 Zeta potential은 원수탁도가 5NTU일 경우 Alum, PAC 및 PACS 모두 -20mV∼-15mV사이였으며, 원수 탁도가 10NTU인 경우에는 0∼0.5mV 범위에 있는 것으로 나타나 응집제 종류 및 주입량이 상이하더라도 응집효율이 가장 양호한 상태에서의 Zeta potential은 일정한 범위내에 있는 것으로 나타났다.

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인라인 혼화 및 응집 시스템의 성능특성 (Performance characteristics of inline mixing and coagulation system)

  • 김동준;박상규;양희천
    • Journal of Advanced Marine Engineering and Technology
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    • 제38권3호
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    • pp.269-275
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    • 2014
  • 본 연구는 PI 개념에 근거한 수처리용 인라인 혼화 및 응집 시스템의 성능특성에 대한 실험적 연구를 목적으로 한다. 3단 인라인 혼화 및 응집 시스템은 처리 원수 저장조, 응집제 주입 정량펌프, 혼화 및 응집관, 침전조 및 제어 판넬로 구성된다. 동일한 응집제와 응집보조제의 주입량 조건에서 응집제의 증가에 따른 탁도 제거율에 비해 응집보조제의 증가에 따른 탁도 제거율이 약 3배 정도 높게 나타났다. 동일한 혼화 및 응집 시간 조건에서 인라인 방식이 기계식에 비해서 평균적으로 약 4.6배 정도 탁도 제거율이 높게 나타났다.