• Journal of Microbiology and Biotechnology
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• 제26권10호
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• pp.1765-1773
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• 2016

Wastewater containing kraft lignin (KL) discharged from pulp and paper industries could cause serious environmental contamination. Appropriate effluent treatment is required to reduce the pollution. Investigations on anaerobic bacteria capable of degrading KL are beneficial to both lignin removal and biofuel regeneration from the effluent. In this paper, an anaerobic strain capable of degrading KL was isolated from the sludge of a pulp and paper mill and identified as Dysgonomonas sp. WJDL-Y1 by 16S rRNA analysis. Optimum conditions for KL degradation by strain WJDL-Y1 were obtained at initial pH of 6.8, C:N ratio of 6 and temperature of 33℃, based on statistical analyses by response surface methodology. For a 1.2 g/l KL solution, a COD removal rate of 20.7% concomitant with biomass increase of 17.6% was achieved after 4 days of incubation under the optimum conditions. After the treatment by strain WJDL-Y1, KL was modified and degraded.

• 상하수도학회지
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• 제25권6호
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• pp.971-979
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• 2011

Palm Oil Mill Effluent (POME) is the mixed organic wastewater generated from palm oil industry. In this study, kinetic analysis with treating POME in an anaerobic hybrid reactor (AHR) was performed. Therefore, the AHR was monitored for its performances with respect to the changes of COD concentrations and hydraulic retention time (HRT). Batch tests were performed to find out the substrate removal kinetics by granular sludge from POME. Modified Stover Kincannon, First-order, Monod, Grau second-order kinetic models were used to analyze the performance of reactor. The results from the batch test indicate that the substrate removal kinetics of granular sludge is corresponds to follow Monod's theory. However, Grau second-order model were the most appropriate models for the continuous test in the AHR. The second order kinetic constant, saturation value constant, maximum substrate removal rate, and first-order kinetic constant were 2.60/day, 41.905 g/L-day, 39.683 g/L-day, and 1.25/day respectively. And the most appropriate model was Grau second-order kinetic model comparing the model prediction values and measured COD concentrations of effluent, whereas modified Stover-Kincannon model showed the lowest correlation.

• 유기물자원화
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• 제27권2호
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• pp.13-18
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• 2019

생활의 향상 및 도시화로 인하여 국내의 하수슬러지는 매년 증대되고 있으나, 해양투기 금지 및 최종처리의 한계로 자원화 방법 중 하나인 혐기성소화의 관심도가 높아지고 있다. 그러나 하수의 고도처리에 따른 혐기성 소화 효율의 한계로 이를 높이기 위한 가용화 기술에 대한 연구가 활발히 진행되고 있다. 특히 가용화 방법 중 경제적이고 유용한 기술로 알려진 오존은 스컴이 다량 발생되고, 제거에 대한 한계성이 있다. 따라서 본 연구에서 소화슬러지의 습식분쇄에 따른 성상변화 및 오존반응의 전처리로 적용 시 스컴의 발생 및 가용화 효율변화를 알아보고자 한다. 연구결과, 습식분쇄만으로 VS/TS는 4.4%, $SCOD_{cr}/TCOD_{cr}$이 9.4% 증대되어 가용화가 일어났다. 또한, 습식분쇄 적용에 따른 오존반응 시 슬러지의 고형분의 입경 감소에 따른 비표면적의 증가로 오존반응만한 경우에 비하여 스컴 발생속도는 14.3% 감소되고, VS/TS는 2.1% 증대 되었다. 이 때 가용화 효율도 23.3% 증가되는 것으로 나타났다. 이러한 결과로 볼 때, 본 연구를 통해 습식분쇄를 적용하여 오존반응 시 슬러지 중의 고형물과 접촉효율이 증가로 스컴의 생성 억제 및 가용화 증대로 후속공정인 혐기성 소화의 효율을 증대시킬 수 있을 것으로 기대된다.

• 환경위생공학
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• 제14권3호
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• pp.31-38
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• 1999

The purpose of this study were to determine the optimum mixing ratio of sewage sludge and papermill sludge as carbon source required to SRB in treating abandoned mine drainage with natural purification wetland. If mixing sewage sludge/papermill sludge 2.0 SO42- reduced 46.2%, and then 30% in mixing ratio 0.5.Because sewage sludge was faster biodegradability than papermill sludge, effluent SCOD was 40mg/L in mixing ratio 0.5, and after that was all but regular. pH and ORP were almost neutral and -160mV, but after that was all but regular and it indicated that SRB activity was suitable. Fe removal rate was 60% in mixing ratio 2.0, and 54% in mixing ratio 0.5. In point of carbon source supply, It indicated that mixing ration 0.5 was considered as the most appropriate, because degradability of swewage sludge under short time was higher than that of papermill sludge.

• 한국수소및신에너지학회논문집
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• 제19권2호
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• pp.145-155
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• 2008

This paper deals with an economic evaluation of hydrogen production by fermentation. We evaluate the economic feasibility of domestic hydrogen production by fermentation utilizing glucose and waste water sludge in terms of hydrogen production prices. In addition, we make some sensitivity analysis of hydrogen prices by changing the values of input factors such as the price of glucose, the capital cost of the hydrogen production system, and the hydrogen production yields. The estimated hydrogen prices of the two-step dark-light hydrogen production by fermentation utilizing glucose was $5,347won/kgH_2$, and the single-step hydrogen production by anaerobic fermentation utilizing waste water sludge was $4,255won/kgH_2$, respectively. It is expected that the hydrogen production price by anaerobic fermentation can be reduced if we produce methane or hydrogen utilizing by-products such as alcohols and organic acids, or the government imposes some legal regulations on the treatment of waste water sludge.

• 상하수도학회지
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• 제26권5호
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• pp.629-636
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• 2012

This study focuses on the feasibility of bio-gas production using anaerobic digestion by measuring methane generation and biodegradability through the BMP test of industrial organic wastes. Organic wastes consist of entrails of pigs and organic residues of rumen generated from slaughter houses, wastewater sludge from slaughter waste water, fish offal and residues of vegetables from public wholesale markets, and wastewater sludge from the process of wastewater treatment in paper mill. The cumulative methane production by BMP test ranges from 149.3 ml/g-VS to 406.6 ml/g-VS and this is similar to methane generation of the normal wastewater sludge and food waste. As a result of measurement of biodegradability, wastewater sludge (S1 ~ S4) is low, ranging from 27.1% to 58.9 % and organic residues of rumen (G1) is low at 49.6 %. In conclusion, it turned out that raising the hydrolysis by various pre-treatments is necessary in order to produce bio-gas by using industrial organic wastes.

• Membrane and Water Treatment
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• 제15권1호
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• pp.1-9
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• 2024

Biological nutrient removal is gaining increasing attention in wastewater treatment plants; however, it is adversely affected by low temperatures. This study examined temperature effects on nutrient removal and morphological stability of the granular and denitrifying phosphorus accumulating organisms (PAO and DPAO, respectively) using sequencing batch reactors (SBRs) at 5, 10, and 20 ℃. Lab-scale SBRs were continuously operated using anaerobic-anoxic and anaerobic-oxic cycles to develop the PAO and DPAO granules for 230 d. Sludge granulation in the two SBRs was observed after approximately 200 d. The average removal efficiency of soluble chemical oxygen demand (SCOD) and PO₄^3--P remained >90% throughout, even when the temperature dropped to 5 ℃. The average removal efficiency of NO₃^--N remained >80% consistently in DPAO SBR. However, nitrification drastically decreased at 10 ℃. Hence, the removal efficiency of NH₄⁺-N was decreased from 99.1% to 54.5% in PAO SBR. Owing to the increased oxygen penetration depth at low temperatures, the influence on nitrification rates was limited. The granule in DPAO and PAO SBR was observed to be unstable and disintegrated at 10 ℃. In conclusion, morphological characteristics showed that changed conversion rates at low temperatures in aerobic granular sludge altered both nutrient removal efficiencies and granule formation.

• 한국물환경학회지
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• 제34권1호
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• pp.121-131
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• 2018

Domestic sewage treatment plants (STPs) consume about 0.5 % of total electric energy produced annually, which is equivalent to 207.7 billion Korean won per year. To minimize the energy consumption and as a way of mitigating the depletion of energy sources, the sewage treatment strategy should be improved to the level of "energy positive". The core processes for the energy positive sewage treatment include A-stage for energy recovery and B-stage for energy-efficient nitrogen removal. The integrated process is known as the A/B-process. In A-stage, chemically enhanced primary treatment (CEPT) or high rate activated sludge (HRAS) processes can be utilized by modifying the primary settling in the first stage of sewage treatment. CEPT utilizes chemical coagulation and flocculation, while HRAS applies returned activated sludge for the efficient recovery of organic contents. The two processes showed organic recovery efficiencies ranging from 60 to 70 %. At a given recovery efficiency of 80 %, 17.3 % of energy potential ($1,398kJ/m^3$) is recovered through the anaerobic digestion and combustion of methane. Besides, anaerobic membrane bioreactor (AnMBR) can recover 85% of organic contents and generate $1,580kJ/m^3$ from the sewage. The recovered energy is equal to the amount of energy consumption by sewage treatment equipped with anaerobic ammonium oxidation (ANAMMOX)-based B-stage, $810{\sim}1,620kJ/m^3$. Therefore, it is possible to upgrade STPs as efficient as energy neutral. However, additional novel technologies, such as, fuel cell and co-digestion, should be applied to achieve "energy positive" sewage treatment.

• 유기물자원화
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• 제11권3호
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• pp.60-66
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• 2003

본 연구는 혐기성 소화를 이용한 음식물쓰레기와 하수슬러지 병합처리를 위한 음식물쓰레기 전처리 공정 방안을 모색하기 위하여 수행되었다. 음식물쓰레기 전처리 공정에 따른 음식물쓰레기 단위 공정별 성상 변화와 산발효조 적정 투여 기초조사 및 음식물쓰레기와 하수슬러지 혼합비 특성변화를 통한 산발효조의 효율 향상방안을 검토하였다. 연구결과, 음식물쓰레기의 구성성분은 대부분이 곡류와 채소류로 산발효 공정에서 유기산으로 전환될 가능성이 충분한 것으로 판단되며, 산발효조 투입시 TS의 적정한 범위를 위한 음식물쓰레기와 희석수의 비율은 1:5가 적합한 것으로 나타났다. 음식물쓰레기 분쇄 후 입도 분포 특성을 고려할 때 약 8mm 이하의 입자가 적합하며, 음식물쓰레기와 하수슬러지 슬러지의 혼합비는 3:7 이하가 적합한 것으로 나타났다.

• 유기물자원화
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• 제17권3호
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• pp.82-90
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• 2009

본 연구에서는 기계식 전처리에 의한 하수 슬러지의 가용화 효과를 회분식 실험을 통해 조사하였다. 기계식 전처리를 통한 하수슬러지의 가용화는 세포벽의 파괴로 통해 용존성 화학적 산소요구량, 단백질 및 탄수화물의 농도를 증가시키는 것으로 나타났다. 알칼리와 기계식 전처리를 병행하여 슬러지를 가용화한 결과 기계식 전처리만을 수행한 경우에 비해 용존성 화학적 산소요구량이 높은 것으로 나타났다. 혐기성 생분해도 측면에서 기계식 전처리는 메탄 발생량을 증가시키는 것으로 나타났다. 기계식과 알칼리 및 기계식 전처리를 동시에 수행한 경우 각각 24.1%와 44.5%의 생화학적 메탄 잠재능을 향상시키는 것으로 나타나 하수슬러지의 가용화는 혐기성 생분해도 향상에 효과적이다.