• 제목/요약/키워드: SBR Process

검색결과 162건 처리시간 0.028초

낮은 C/N 비에서 운영되는 SBR 유형의 Two-Sludge 공정의 질소 제거 특성 (Nitrogen Removal Characteristics in Two-Sludge System of SBR Type Using Sewage Wastewater of Low C/N Ratio)

  • 류홍덕;김학인;이상일
    • 대한환경공학회지
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    • 제28권1호
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    • pp.7-14
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    • 2006
  • 본 연구에서는 도시하수를 이용하여 two-sludge 시스템방식의 SBR3 공정의 질소제거 효율 향상능을 평가하기 위해 기존 재래식 SBR 공정(SBR1) 및 분할주입(step-feeding)을 통해 탈질효율 향상을 도모한 SBR2 공정과의 비교 연구를 수행하였다. 도시하수를 대상으로 한 연구결과 two-sludge 시스템 방식으로 질산화 반응이 별도의 반응조에서 진행되며(external nitrification), 질산화된 질산염은 생흡착된 유기물을 이용하여 효과적으로 탈질되는 SBR3 공정이 SBR1 및 SBR2 반응조에 비해 T-N 제거효율면에서 우수함이 관찰되었다. SBR3 공정과 SBR1 및 SBR2 공정의 T-N 제거효율 차이는 낮은 C/N 비에서 더 크게 관찰되었으며 이는 생흡착 기작을 이용하는 SBR3 공정이 SBR1 및 SBR2 공정에 비해 탈질시 유기물 이용을 효율적으로 함을 의미한다. SBR3 공정은 T-N 유입 부하율에 따른 T-N 제거효율 관계에서도 SBR1 및 SBR2 공정에 비해 성능이 우수함을 관찰할 수 있었다. SBR3 공정이 SBR1 및 SBR2 공정에 비해 높은 T-N 부하율에서도 질소제거효율이 높은 원인은 SBR3 공정이 two-sludge 시스템 방식으로 운영됨에 따라 질화박테리아가 독립된 반응조에서 질산화를 수행하므로(external nitrification) 질산화 반응시 소요되는 수리학적 체류시간을 단축시킬 수 있기 때문이다.

SBR 및 BS-SBR 처리의 공정변화 연구 (Process variations in SBR and BS-SBR treatment)

  • 양형재;정윤철;신응배
    • 환경위생공학
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    • 제12권1호
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    • pp.59-68
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    • 1997
  • 이 연구에서는 SBR에 Rotating disks를 부착하여 회전하면서 두 원판 사이에서 전단력이 발생하는 BS-SBR을 이용하여 용해성 유기물질 제거율과 슬러지 분리에 대해 비교 검토하였다. BS-SBR 공정에서는 부유성 활성슬러지와 생물학적 고정막에 대해 동시처리 되어 높은 처리효율을 보였다. SCOD 제거율은 SBR보다 높은 97%를 보였다. 처리수의 평균 SS 농도는 $4.8mg/{\ell}$ 정도로 나타났고, 1-cycle/d 및 3-cycle/d 모두 $10mg/{\ell}$ 이하를 유지하여 매우 효과적임을 알 수 있었다. 슬러지 침전 특성은 SBR과는 상이한 매우 좋은 결과를 보였다. 운전 중 슬러지는 진한 갈색으로 플록이 잘 형성되었고, 그 크기는 SBR에서 보다 크다는 것이 눈으로 확인할 수 있을 정도였다.

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Influence of Process Oil Content on Properties of Silica-SBR Rubber Compounds

  • Kim, Jung Soo;Kim, Dong Hyun
    • Elastomers and Composites
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    • 제55권3호
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    • pp.184-190
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    • 2020
  • In the wet master batch process, process oil is used to improve the workability of silica-SBR. The process oil expands the polymer and provides lubrication to soften the stiff rubber chain. However, addition of excess process oil can interfere in the crosslinking reaction between rubber molecules and reduce the crosslinking density of silica-SBR. Controlling the amount of process oil is an important aspect for properly controlling the workability and crosslinking density of silica-SBR. In this study, silica-SBR was prepared by adjusting the amount of process oil to confirm its effect on silicaSBR. Vulcanization characteristics of silica-SBR were examined using a moving die rheometer. Dynamic viscoelasticity was measured using a dynamic mechanical thermal analyzer, and the mechanical properties were investigated using the universal testing machine according to ASTM D412. As a result, all silica-SBR compounds with 10 to 40 phr of process oil have effects of improving the processability and the silica dispersibility. Also, the optimum condition was determined when 10 phr of processed oil was added because the abrasion resistance was improved 65% compared to that at 40 phr.

Treatment of High Concentration Organic Wastewater with a Sequencing Batch Reactor (SBR) Process Combined with Electro-flotation as a Solids-liquid Separation Method

  • Choi, Younggyun;Park, Minjeong;Park, Mincheol;Kim, Sunghong
    • Environmental Engineering Research
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    • 제19권4호
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    • pp.395-399
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    • 2014
  • Operation characteristics of the sequencing batch reactor (SBR) process with electro-flotation (EF) as a solid liquid separation method (EF-SBR) were investigated. EF-SBR process showed excellent solid-liquid separation performance which enabled to separate biosolids from liquid phase within 30 min and to extend cyclic reaction time. Although influent organic loading rate was increased stepwise from 5 to 15 g COD/day, food to microorganisms (F/M) ratio could be maintained about 0.3 g COD/g VSS/day in EF-SBR because biomass concentration could be easily controlled at desired level by EF. However, it was impossible to increase biomass concentration at the same level in control SBR (C-SBR) process because solid-liquid separation by gravity settling showed a limitation at higher mixed liquor suspended solids (MLSS) concentration with 60 min of settling time. Total chemical oxygen demand (TCOD) removal efficiency of EF-SBR process was not decreased although influent organic loading rate became 3 times higher than initial value. However, it was seriously deteriorated in C-SBR process after increasing the rate over 10 g COD/day, which was accounted for insufficient organic removal by relatively higher food to microorganisms (F/M) ratio as well as biosolids wash-out by a limitation of gravity sedimentation.

RO 농축수 처리를 위한 SBR과 MLE 공정의 비교 평가 (A comparative study on SBR and MLE Process for RO Retentate Treatment)

  • 김일회;이상일
    • 상하수도학회지
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    • 제25권6호
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    • pp.907-915
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    • 2011
  • In this study, the SBR and MLE process was performed for a removal of the RO retentate and the nitrogen removal efficiency was evaluated. The inflow-rate of two processes was set a 10 L/day. The SBR process was operated a two cycle as HRT per one cycle was 12hr and the HRT of the anoxic and aerobic tank was respectively 7.5 hr and 16.5 hr. The methanol was injected for an effective denitrificaion owing to a low C/N ratio of the RO retentate. The two processes were effectively performed for nitrogen removal, but the average removal efficiency of the SBR process was about 94.93% better performance than the MLE process. Therefore, the SBR process demonstrated a good performance more than the MLE process for nitrogen removal of the RO retentate. The kinetic of SNR and SDNR was observed respectively 0.051 kg $NH_{3}-N/kg\;MLVSS{\cdot}dayg$ and 0.287 kg ${NO_3}^--N/kg\;MLVSS{\cdot}day$, which will be useful to design for the wastewater treatment system with a RO retentate.

RO 농축수 처리를 위한 SBR 공정 적용에 관한 연구 (A Study on Application of SBR Process for RO Retentate Treatment)

  • 김일회;주현종
    • 대한환경공학회지
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    • 제34권2호
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    • pp.79-85
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    • 2012
  • 본 연구는 역삼투공정에서 발생하는 농축수의 생물학적 처리에 관한 것으로, SBR공정의 처리성능 및 부하변동과 온도변화에 따른 효율을 평가하였다. SBR공정의 cycle당 HRT가 각각 8시간과 12시간으로 2가지 형태로 공정운전이 이루어졌으며, RO농축수의 낮은 C/N비 때문에 효과적인 탈질을 위해 메탄올을 주입하였다. 유량과 온도의 변화에도 SBR공정의 질소제거 효율은 비교적 안정적인 것으로 나타났다. SBR공정의 최적 time cycle은 2 cycle/day이지만, 3 cycle/day 조건에서도 방류수 TN 농도가 수질기준 이하로 나타났다. 평가결과 RO 농축수 처리를 위한 SBR공정의 적용은 효과적이었으며, 폐수처리장 설계에 활용이 가능할 것이다. SNR과 SDNR은 각각 $0.043{\sim}0.066kg\;NH_3-N/kg\;MLVSS{\cdot}day$$0.096{\sim}0.287kg\;NH_3^--N/kg\;MLVSS{\cdot}day$로 나타났다. 도출된 동역학적인자는 RO농축수 처리에서 포기조와 무산소조 설계에 적용이 가능할 것이다.

유전자 알고리즘 기반 다항식 뉴럴네트워크를 이용한 비선형 질소제거 SBR 공정의 모델링 (Modeling of Nonlinear SBR Process for Nitrogen Removal via GA-based Polynomial Neural Network)

  • 김동원;박장현;이호식;박영환;박귀태
    • 제어로봇시스템학회논문지
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    • 제10권3호
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    • pp.280-285
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    • 2004
  • This paper is concerned with the modeling and identification of sequencing batch reactor (SBR) via genetic algorithm based polynomial neural network (GA-based PNN). The model describes a biological SBR used in the wastewater treatment process fur nitrogen removal. A conventional polynomial neural network (PNN) is applied to construct a predictive model of SBR process fur nitrogen removal before. But the performances of PNN depend strongly on the number of input variables available to the model, the number of input variables and type (order) of the polynomials to each node. They must be fixed by the designer in advance before the architecture is constructed. So the trial and error method must go with heavy computation burden and low efficiency. To alleviate these problems, we propose GA-based PNN. The order of the polynomial, the number of input variables, and the optimum input variables are encoded as a chromosome and fitness of each chromosome is computed. Simulation results have shown that the complex SBR process can be modeled reasonably well by the present scheme with a much simpler structure compared with the conventional PNN model.

퍼지 시스템을 이용한 비선형 질소제거 SBR 공정의 모델링 (Modeling of Nonlinear SBR Process for Nitrogen Removal Using Fuzzy Systems)

  • 김동원;박장현;이호식;박영환;박귀태
    • 한국지능시스템학회논문지
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    • 제14권2호
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    • pp.190-194
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    • 2004
  • 본 논문에서는 비선형 생화학적인 공정의 모델링을 위해 퍼지시스템이 응용된 것을 보인다. SBR 반응조에서 질소제거를 위한 수처리 공정이 제시되었으며, 이 공정의 ORP값을 모델링하고 동정하기 위해 서로 다른 후반부 다항식을 가진 퍼지시스템이 소개되었다. 퍼지모델링 결과를 비교하고 분석하며 또한 제안된 방법에 의해 비선형 공정이 합리적이고 효율적으로 모델링 될 수 있음을 본 논문에서 보인다.

전해부상을 고액분리 방법으로 적용한 SBR 공정의 운전 특성 (Operation Characteristics of the SBR Process with Electro-Flotation (EF) as Solids-liquid Separation Method)

  • 박민정;최영균
    • 한국물환경학회지
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    • 제24권3호
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    • pp.340-344
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    • 2008
  • Electro-flotation (EF) was applied to a sequencing batch reactor process (SBR) in order to enhance solids-liquid separation. Solids-liquid separation was good enough in the SBR coupled with EF (EF-SBR) and it was possible to maintain the concentration of mixed liquor suspended solids (MLSS) high in the EF-SBR. Under moderate organic loading condition (COD loading rate: 6 g/day), control SBR (C-SBR) showed similar treatment efficiencies with the EF-SBR. Under high organic loading condition (COD loading rate: 9.6 g/day), the solids-liquid separation in the C-SBR was deteriorated due to proliferation of filamentous bulking organisms at high F/M ratio. However, the EF-SBR was operated stably and with the high MLSS concentration (above 4,000 mg/L) regardless of the organic loading conditions during overall operating period leading to the satisfactory effluent quality. Gas production rate of the electrodes was gradually decreased because of anodic corrosion and scale build-up at the surface of cathode. However it could be partially overcome by use of corrosion-proof electrode material (SUS-316 L) and by periodic current switching between the electrodes.

Properties of Silica-SBR Compounds Using Cellulose Dispersant Applicable to Tire Tread Rubber

  • Kim, Jung Soo;Kim, Dong Hyun
    • Elastomers and Composites
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    • 제55권3호
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    • pp.176-183
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    • 2020
  • Silica-styrene butadiene rubber (Silica-SBR) compounds have been used in the preparation of tire treads. The silica dispersibility of silica-SBR compounds is related to the processability, mechanical properties, and wear resistance of tires. Recently, in order to improve the silica dispersibility of the silica-SBR compounds, the wet masterbatch (WMB) process was introduced, which is a method of mixing rubber in the water phase. We aimed to improve the silica dispersibility of the silica-SBR compounds by preparing a silica dispersant applicable to the WMB process. For this purpose, cellulose, 2-hydroxyethyl cellulose, and cellulose acetate were employed as a silica dispersant. The silica dispersibility of the compounds was measured by a moving die rheometer. Improvement in the processability of silica-SBR compounds was evaluated by the Mooney viscometer. The wear resistance of silica-SBR compounds using a cellulose dispersant was improved by up to 29%.