• Journal of the Korean Wood Science and Technology
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• 제48권3호
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• pp.271-282
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• 2020

하수처리장은 도시를 구성하는 사회기반시설물로 2017년 하수도 통계 기준 국내 하수도 보급률은 94%에 달하고 있다. 국내 하수처리장에서 PAC(Poly Aluminum Chloride)의 사용량이 58%를 차지하고 있으나 PAC의 경우 품질기준상 불순물(중금속) 함량이 높음에도 불구하고, 기준 강화나 기술적 품질개선이 제대로 이루어지지 않아 응집제 과다 주입 시 2차 오염문제가 대두되고 있다. 또한, 약품사용량이 증가함에 따라 2017년 기준 연간 하수슬러지 발생량과 슬러지 재이용의 필요성 또한 증대되고 있다. 이에 본 연구에서는 반탄화목분 천연재료 혼합응집제를 이용한 수처리 시 혼합응집제 주입에 따른 중금속류에 대한 안정성을 평가하고, 하수슬러지의 침강성 및 하수슬러지 발열량 평가를 통해 슬러지 재이용의 가능성을 검증하고자 한다. 반탄화목분 천연재료 혼합응집제와 PAC(10%)의 중금속류(Cr, Fe, Zn, Cu, Cd, As, Pb, Ni) 분석 결과 Cr, Cd, Pb, Ni, Hg의 경우 검출되지 않았으며, Zn의 경우 반탄화목분 천연재료 혼합응집제에서 먹는물 수질기준에서 고시한 Zn의 농도가 3mg/L인 것에 비해 0.007 mg/L로 극소량만 검출되었다. Fe, Cu, As의 경우 PAC(10%)를 주입한 경우가 반탄화목분 천연재료 혼합응집제 보다 최대 2배 이상 검출되는 것으로 나타났다. 또한, 슬러지 침강성 분석 결과 반탄화목분 천연재료 혼합응집제가 기존 응집제인 PAC(10%)에 비해 최대 2배 빠르게 침강하는 것으로 반탄화목분 혼합응집제의 침강성이 PAC(10%)보다 우수한 것으로 나타났다. 반탄화목분 천연재료 혼합응집제를 주입하여 발생된 하수슬러지의 건조기준 저위발열량은 3,378 kcal/kg이며, PAC(10%) 응집제를 주입하여 발생된 하수슬러지의 건조기준 저위발열량은 3,171 kcal/kg으로 두 응집제 모두 화력발전소의 보조연료 구비조건을 만족하였으나, 본 연구에서 개발한 반탄화목분 천연재료 혼합응집제를 사용할 경우 기존의 응집제보다 200 kal/kg 정도 높은 슬러지 발열량을 확보할 수 있음을 확인하였다. 따라서, 반탄화목분 혼합응집제를 이용하여 수처리를 수행할 경우 기존의 응집제인 PAC(10%)보다 중금속류에 대해 안정적이며, 우수한 슬러지 침강성과 높은 발열량을 갖는 슬러지를 생성하여 환경적으로 안정적이며, 효율적인 활용이 가능할 것으로 판단된다.

• 상하수도학회지
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• 제22권4호
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• pp.449-454
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• 2008

Some pretreatment methods have been proposed to enhance the biodegradability and to shorten the hydrolysis reaction time. By means of efficient pretreatment the suspended solids (SS) can be made of better accessible for the anaerobic bacteria. There are several ways how this can be accomplished, which include biological, mechanical, thermal, and chemical methods. For the sludge solubilization using the cavitation phenomenon, we have tried to develop a pretreatment process consisted of a reactor and pumps. The objectives of this study were to develop a advanced wastewater treatment consisted of IABR and the cavitation with PGA. The most effective removal for organic matter and nutrients were occured when both cavitation pretreatment and ${\gamma}$-PGA were applied at the IABR process. Only small portion of ${\gamma}$-PGA at a rate of 1.38mg/L, was enough to improve sedimentation ability, SS removal efficiencies, and sludge volume reduction. After the sludge solubilization by the cavitation, SCOD increased to 193% and SS decreased to 36%. The removal ratio of BOD was 94.5%, T-N removal ratio was 85.5% and T-P removal ratio was 84.9%. The combination process of the IABR with the cavitation and PGA addition seems to be very effective alternative wastewater treatment process.

• 한국환경보건학회지
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• 제20권2호
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• pp.28-38
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• 1994

New problems have been recently posed on the abnormal foaming (Scum) in an aeration tank and the sludge flotation in a final sedimentation tank during the activated sludge process. However, the activities of the causing bacteria, Nocardia-amarae in an aeration tank have not been searched out at all. Therefore, in this article the activities of Nocardia-amarae in an aeration tank have been closely examined by means of the changes of (F/M) ratio, SRT and inflowing substrate using continuous type and fed-batch type. Summarized results of experiments are as follows. 1. Regrading continuous culture when synthetic wastewater was used substrate neither the increase in the number of Nocardia-amarae in the aeration tank nor the Occurrence of Scum was observed. 2. In the case of fed-batch culture, Nocardia-amarae in the aeration tank increased due to the partial change in substrate and the effect of SRT was significant. 3. Once the scum was formed and the quantity of added Nocardia-amarae and substrate were not changed, the effect of STR was not significant.

• 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.

• 펄프종이기술
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• 제34권3호
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• pp.32-37
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• 2002

The paper mill wastewater actually generating bulking was used to apply to the spot. Batch and continuous type pilots were used in this study. Optimal time after propagating generation of activated sludge in aeration basin by adding Hoc forming microorganism was 24 and 36hours while optimal time of activated sludge in original aeration basin was 60hours. Showing the difference of sedimentation velocity at 7th day after operating a pilot continuously, SV30 was decreased to 50% at 13th day. COD value in aeration basin with floe forming microorganism was 35mg/L while COD value in original aeration basin was 52mg/L. It was indicated that application of Hoc forming microorganism can control the bulking of paper mill wastewater by shortening of recovery time and improving of pollution removal efficiency.

• 한국초전도ㆍ저온공학회논문지
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• 제23권3호
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• pp.20-25
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• 2021

Milking parlor wastewater contains high concentration suspended solid (SS), nitrogen, and/or phosphate as well as organic compounds. A new biological wastewater process by magnetic separation, magnetic activated sludge (MAS) process, was applied to milking parlor wastewater treatment process. A three step wastewater treatment process of coagulation sedimentation / ammonia stripping (C/S), magnetic activated sludge process and contact oxidation (CO) was proposed for removal of these pollutants. First step, C/S process recovered 96% TN and 96% PO₄^3--P as resource for fertilizer from the wastewater. 81% biochemical oxygen demand (BOD) in wastewater was removed after MAS process. As a results, all pollutant concentrations satisfied Japanese effluent standards. Most of residual BOD and SS were removed by the CO process. It was estimated that the proposed process could reduce the process space to 1/7.

• 한국산학기술학회논문지
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• 제8권3호
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• pp.627-631
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• 2007

슬러지의 침전성에 영향을 미치는 인자는 F/M비, 유입수의 성분과 조성, 처리수온, 포기조의 pH, 슬러지 일령, 사상성세균의 증식 등으로 알려져 있으며, 유기산의 잔류량이 EPS의 분비에 영향을 미쳐 슬러지의 침강성에 영향을 주게 된다. 바실러스를 이용한 공법에서 생물 반응조는 특히 바실러스 종의 우점화를 위한 포자화의 진행을 이루는데 중요한 것으로 알려져 있으나 이에 대한 기작 설명은 아직 미흡한 실정이다. 바실러스를 이용한 B3 공법과 RABC 공법으로 운전 중인 처리장의 생물반응조는 점감포기를 하고 있으며 침전조에서 포자를 형성한 바실러스가 생물반응조로 반송되면 1.6mg/L로 높아진 DO농도와 유기물질 유입으로 바실러스가 발아를 하고 활성도가 높아지며, 0.5mg/L로 낮아진 DO농도로 인하여 포자를 형성하면 EPS 추출물질 중 Protein의 함량이 109.95mgEPS/gSS에서 131.77 mg EPS/gSS로 증가하고 SVI는 85mL/g에서 96mL/g사이로 양호함에 따라 DO농도가 EPS 추출물질 중 Protein의 생성에 영향을 미치며 Protein의 함량이 침전에 영향을 미치는 것으로 판단된다. 또한 Protein/Carbohydrate 비율에 따라 침강성은 영향을 받는 것으로 나타났다. 특히 RABC 공법에서는 Protein/Carbohydrate의 비가 침전에 영향을 미치는 것으로 나타난 반면, B3 공법에서는 Protein/carbohydrate의 비에 영향을 크게 받지 않는 것으로 나타났다.

• 한국지반공학회:학술대회논문집
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• 한국지반공학회 2008년도 추계 학술발표회
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• pp.1446-1451
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• 2008

The clay found in the river or in any waste water treatment plant usually have a very high content of water. A large amount of sediments hinder the navigation in river. In waste water treatment plant, there is requirement of settling the thick sludge. These problems are overcome by using rapid means of sedimentation and settling. This paper focus on how method of Electrokinetic sedimentation can be made faster. Sedimentation using Electrokinetic phenomenon has been discussed with varied voltage applied and effect and dose of coagulant in increasing the process. The experimental test has been carried out at water content that are generally present in the case of river and small canals carrying waste water. This paper also focus on different heavy metals concentration during the process and the power aspects of process. A series of experiment were done to support the proposed theory and how a bubble formation could hinder the purpose of experiment.

• 기술사
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• 제18권3호
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• pp.28-35
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• 1985

As the paper industry consumes much water in process and discharge wastewater containing suspended solid and COD(chemical oxygen demand), relevant law against this discharge has been set up to limit the total containment of COD in discharge. This study has been carried out to improve the treatment method for the soluble COD in wastewater produced during the process of paste-board production, which is made of semichemical pulp and waste paper. Applicated methods are, O$_2$AS : O$_2$ activated sludge process DAS : Deep well activated sludge process SAS : standard activated sludge process and proper combination of DAS and SAS 1) As a result of this experiment, we get the following conclusion between in COD sludge loading "X" and COD removable rate in the process of treating waste-water. COD removable rate(％)=(0.778+0.0146/X)${\times}$100(％)……(7) 2) In case that the COD sludge loading is high, it has been cleared out that the COD removable rate shall become low due to unknown unsoluble substances contained in the process. Meanwhile, to increase the efficiency rate of treatment, it is thought to be necessary, to provide long-time contacts with activated sludge. 3) Once the COD of original waste-water and the target COD of treated water are decided, COD sludge loading is obtained from equation(7), and capacity of aeration tank in the effective systems such as O$_2$AS, DAS, to bet the required COD removable rate can be decided. Therefore the choice among SAS, O$_2$AS, DAS methods is made in consideration of required COD removable rate and allowable installation area. 4) In the sedimentation tank with sludge bulking, it is possible to increase the COD removable rate by 3～7％ but still there exist many obstacles to manage this operation.

• 청정기술
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• 제7권1호
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• pp.35-42
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• 2001

본 연구에서는 zeolite를 활성슬러지 공정에 주입할 경우 zeolite가 biofloc에 미치는 영향에 대해 알아보기 위해 수행되었다. 두 반응기를 동일 조건으로 운전하였으며 하나는 표준 활성슬러지 공정 (CU)으로, 다른 하나는 zeolite를 폭기조내 4,000 mg/l로 유지 (ZU)하며 비교하였다. 슬러지 플럭 입경을 측정한 결과, 두 반응기 모두 SRT (Solid Retention Time)가 증가함에 따라 플럭 크기도 비례하여 증가하였으나 ZU가 모든 조건에서 CU보다 작은 평균 입경을 나타내었다. 한편, 두 반응기에 대해 슬러지 침전성을 비교한 결과, ZU는 SRT변화에 관계없이 3.4~11m/h의 침전속도를 나타내며 SVI(Sludge Volume Index)도 50~108 ml/g으로 양호한 침전상태를 보였다. 그러나 CU는 SRT 증가에 따라 슬러지 침전성이 큰 영향을 받았고 SRT 40일에서 Sphaerotilus가 우점종을 나타내었으며 이 결과, 슬러지가 전혀 침전하지 않았다.