• KSBB Journal
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• v.15 no.4
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• pp.370-374
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• 2000

Some bacterial strains isolated from activated sludges and media and type cultures were cultivated in a pharmaceutical wastewater and a paperboard wastewater and added during batch treatment of those wastewaters in order for these strains to increase the treatment efficiency. Bacillus sp(PC-3) isolated from the charcoal media of the pharmaceutical wastewater plant grew remarkably over there strains in that wastewater and the viable cell count after 24hr cultivation was $1.1{\times}10^6m/L$. Bacillus subtills KCTC 1028 a type strain grew best in the paperboard wastewater and the viable cell count after 24hr cultivation was $1.1{\times}10^7m/L$. Addition of PC-3 in a batch treatment of the pharmaceutical wastewater increased COD removal by 18% after 8 day. And addition of Bacillus subtills KCTC 1028 in a batch treatment of the paperboard wastewater increased COD removal by 14% only after 24hy Bacillus subtills DCTC 1028 was though to be able to be produced economically using alcohol distillery wastewaters from starch material.

• Journal of Korean Society of Water and Wastewater
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• v.20 no.1
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• pp.128-137
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• 2006

This study aims at developing the practical technology in the treatment of box-mill wastewater using the aerobic co-metabolism principle. The conventional activated sludge method exhibited the removal efficiency of $TBOD_5$ and $TCOD_{Mn}$ as 30~50% and 40~50%, respectively. Color was rather increased by 30~130% because the conventional treatment under the aerobic condition did not induce the conversion of molecular structure of dyeing agents. Meanwhile, when the aerobic co-metabolism principle was applied to the same wastewater, the removal efficiency of $TBOD_5$ and $TCOD_{Mn}$ were obtained as 92~97% and 90~94%, respectively. In particular, color was significantly reduced down to 65~85%. The enhancement of treatment efficiency was ascribed to occur not only that the non-degradables were converted to the second substrates, but also that the enzyme activity was increased as MLVSS was kept 3000mg/l or more with the first substrates injected.

• Journal of Korean Society of Environmental Engineers
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• v.28 no.10
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• pp.1090-1097
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• 2006

The anoxic activated sludge process was applied to the treatment of industrial box-mill wastewater, which exhibited the high removal efficiencies of $90{\sim}94%$$ TCOD_{Mn}$ and $58{\sim}81%$ Color. For the design of industrial anoxic activated sludge process, Monod bio-kinetic coefficients of box-mill wastewater were estimated as follows: $K_{max}$(maximum specific substrate removal rate)=0.52 $day^{-1}$, $K_s$(half saturation constant)=314 mg/L, $K_d$(decay coefficient)=0.274 $day^{-1}$, y(microbial yield coefficient)=0.908 mg/mg, and ${\mu}_{max}$(maximum specific growth rate)=0.472 $day^{-1}$. Space loading factors for the design analysis were practically determined as the values of F/M ratio=$0.043{\sim}0.07$ kg-$TCOD_{Mn}$/kg-SS-day, BOD space loading=$0.18{\sim}0.3$ kg-$TCOD_{Mn}/m^3-day$, and ${\theta}_x=6.8{\sim}26.4$ day when considering the relationship of these loading factors with growth dynamics of microorganisms, the F/M ratio that is inversely proportional to ${\theta}_x$ should be equivalent to ${\mu}_{max}$ in units, but exhibited the significant difference between theses two values. Therefore, it is considered that high safety factors are requested in the design of anoxic activated sludge process that is based on Monod bio-kinetics of microorganism.

• Journal of Korean Society of Water and Wastewater
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• v.20 no.3
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• pp.329-338
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• 2006

The research aims to provide the basic data for practical applications by correlating the bio-kinetic coefficients with the load of recalcitrant organic matter in box-mill wastewater. The activated sludge process was employed to a Wastewater disposal plant in an industrial setting, increase of consequently leading to the organic load. The parameter values derived by Monod-kinetic analysis were as follows:specific substrate removal rate $K_{max}=0.17day^{-1}$, half saturation constants $K_s=60.37mg/l$, decay coefficient $K_d=0.142day^{-1}$, microbial yield coefficient y = 0.388mg/mg, and max specific growth rate ${\mu}_{max}=0.006day^{-1}$. In view of biodegradability, the $TCOD_{Mn}/TBOD_5$ ratios of inflow and outflow were 1.07 and 1.41, and the $SCOD_{Mn}/SBOD_5$ ratios of inflow and outflow were 1.10 and 1.50, respectively. The higher $TCOD_{Mn}/TBOD_5$ ratio of outflow indicated that metabolites of a microorganism have accumulated in the cells.

• Proceedings of the Korea Technical Association of the Pulp and Paper Industry Conference
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• 2001.11a
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• pp.44-44
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• 2001

최근들어 환경보호, 자원절약 및 산업의 경제성 확립을 위하여 전세계적으로 자원의 재활 용에 대한 일반 대중의 관심이 고조되고 있으며, 이와 때를 같이하여 각종 재활용 촉진을 위한 법규와 제도가 강화되어가고 있다. 이러한 분위기는 제지산업 분야의 경우 재생펄프 의 사용량 증가로 나타나고 있다. 그 동안 고지를 주된 원료로 사용하던 신문지, 판지 및 라이너지 등의 지종은 고지 사용 비율을 점차 높혀가고 있으며 천연펄프를 주된 원료로 이용하던 고급 인쇄용지와 화장지 분야에도 재생펄프의 사용이 시도되거나 확대되고 있 다. 아울러 전 지종에 걸쳐서 고수율 펄프의 활용 증대를 통한 산림자원 보호 및 경제성 확립에도 많은 노력이 경주되고 있다. 이러한 고지 및 고수율 펄프의 이용 증가 추세는 단 순한 경제적 이유에서 뿐만이 아니라 갈수록 강화되고 있는 환경보전과 자원절감을 달성 하기 위해서 지속되리라고 판단된다. 재생펄프의 이용과 함께 날로 엄격해지는 폐수 배출 규제와 관련하여 제지 공정을 폐쇄 화 방안이 적극 검토되고 있거나 실제로 적용되고 있다. 이에 따라 초지계의 백수 조건이 악화되고 있으며 앞으로 이러한 추세는 심화될 것이 자명하다. 이러한 백수계의 오염은 각종 첨가제의 기능 저하를 유발시키므로 공정 폐쇄화에 대처할 수 있는 새로운 기능성 보류시스템의 개발이 선행되지 않는다면 보류되지 못한 첨가제 혹은 미세분이 초지계를 오염시키는 악순환이 거듭될 것이 자명하다. 따라서 고지 재활용 및 공정 폐쇄화에 적극적으로 대처하기 위해서는 변화되는 원료 및 용수 조건에 능동적으로 대처할 수 있는 새로운 기능성 보류시스템으로서 전분과 마이크 로파티클로 구성된 보류 시스템을 검토하였다. 특히 마이크로파티클 시스템의 구성요소의 하나인 양성전분의 개질에 따른 효과를 평가하기 위해서 다양한 종류의 양성전분을 준비 하고 그 사용에 따른 미세분 보류도, reversibility 등을 측정하였다. 특히 reversibility를 측정함으로써 제지공정상에서의 전단력에 의한 응집에 파괴이후의 재응집 능력을 평가하 였다.

• Journal of the Korean Professional Engineers Association
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• v.18 no.3
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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.