• Journal of Wetlands Research
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• v.15 no.4
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• pp.471-476
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• 2013

The operating conditions of sludge disposal for sanitary paper manufacturing wastewater treatment plant were monitored on the basis of daily check sheets during the 3 years of operation. Generated wastes were mainly composed of 79% of sludge, 14% of ash, 5% of waste synthetic resin and 2% of etc. Maximum sludge was produced to 233 ton and the average was 113 ton daily, where the primary sludge occupied 85% and 15% for the secondary sludge. The concentration of coagulant for sludge dewatering was extremely exceeded and the additional experiment such as jar-test was required for the establishment of proper dosage. Presently, the generated sludges were partially treated outside and were also partly handled inside. In the future, most sludges will be expected to be treated to recycling material for the iron industry.

• Water for future
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• v.25 no.2
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• pp.61-66
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• 1992

This study was to determine the static acute toxicity on Daphnia magna for the Electric cable Factory Wastewater. Activated sludge process was used to treat the wastewater with three different F/M ratios, 0.36, 0.2, 0.1 mg COD/day.mg MLSS. The results of laboratory bioassay with Daphnia magna were as follows. 1)24hr, 48hr-LC$ of the influent were 17.33% and 11.73%. 2)24hr-LC $ of effluents treated with F/M ratio 0.36,0.26 and 0.1mg COD/day.mg MLSS were 26.69% 32.70% and 38.36% respectively, 48-LC$ of these effluents were 14.48% 27.88% and 31.58% respectively. 3)According to various F/M ratios, the ratios of dffluent 48hr-LC$ to filtrated 48hr-LC$ were 1.58, 1.83 and 1.47respectively 4)Activated sludge process effluents treated with activated carbon had little toxicity on Daphnia magna.

• Membrane Journal
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• v.24 no.1
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• pp.63-68
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• 2014

Manufacturing facility for non-alcoholic drink, the parts of the food industry, disposes wastewater which includes high organic concentration and low nitrogen, phosphorus concentration. For this kind of wastewater, the treatment plant consists mainly of aerobic reactor and chemical coagulation process. And sand-filter or activated carbon process is normally installed further. However, aerobic reactor must have long HRT to treat high concentration of organic contaminant included in this wastewater, so the large site area is required. And settling tank which is normally applied for wastewater treatment facility has some problems such as water quality degradation caused by the sludge spill. To solve these problems, we applied MBR system for the wastewater. And the MBR pilot plant was installed nearby the wastewater treatment facility of W food factory and operated during long term to evaluate treatment efficiency. This plant was operated about 3 months and than the result was 97% of organic removal rate on conditions of flow rate $20m^3/day$, HRT 29 hr, recycle 4Q. However, contaminant removal ratio of bio-reactor decreased and TMP of membrane increased rapidly on more conditions.

• Korean Journal of Microbiology
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• v.25 no.4
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• pp.333-338
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• 1987

In order to establish the biological treatment system which can be used for treatment of waste aster from acetaldehyde plant, it was investigated optimum nutrient requirements and growth conditions by mixed culture of Micrococcus roseus AW-6, Micrococcus luteus AW-22, Microbacterium lacticum AW-38 and Microbacterium laevaniformans AW-41 as well as the effect of coagulants and neutralization reagents. Also, it was carried out the continuous culture as well as batch culture to treat the waste water by mixed culture of these strains. The COD removal rate was reached to maximum state for 96hrs culture at pH7.0 and $30^{\circ}C$ NaOH as the neutralization reagents was the most effective, but the coagulants had no effect on the COD remonal rate and the optimum dilution times for treatment were 10 fold. The COD removal rate was also increased by supplimenting 200 ppm $NH_{2}NO_{3}$, 50 ppm $KH_{2}PO_{4}$, 15 ppm $CaCl_{2}$ and 1 ppm $MgSO_{4} \cdot 7H_{2}O $ as additional nutrients. The removal rate coefficient $K_{1}$ on the batch culture was $4.5\times 10^{-6}$, and the detention time for BOD removal rate of 85% was approximately 45hrs. The COD of waste water was reduced to 15% of its initial value by the continuous culture. The COD and BOD of the effluents were to be about 60 ppm and 40 ppm, respectively, and final pH was 7.0.

• Journal of Forest and Environmental Science
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• v.14 no.1
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• pp.101-111
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• 1998

Sedimentation characteristics SS, $BOD_5$ and removal efficiency of waste water in the tissue paper mill using milk carton were examined. Optimum dosage of coagulant, rapid mixing time and slow mixing time were determined by turbidity, SS and S-$BOD_5$ and then equation for treatment efficiency was suggested. For the coagulant, polyaluminium chloride(PAC) are compared with a little better efficiency compare to the aluminium sulfate.

• Korean Journal of Food Science and Technology
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• v.27 no.3
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• pp.318-323
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• 1995

To improve wastewater treatment in a confectionery factory and to optimize chemical coagulation process, this study was performed. $COD_{Mn}$ and total solid of untreated wastewater were $200{\sim}820ppm\;and\;860{\sim}1350ppm$, respectively. Composition of total solid was sugar 40%, protein 10%, hexane-soluble 20%, and ash 30%. Turbidity at 650 nm and the amount of suspended solid (SS) showed correlation, thus turbidity could be used for the on-line measurement of SS. The most effective combination of coagulants for the removal of $COD_{Mn}$ and SS was that of $Al_2(SO_4)_3\;and\;Ca(OH)_2$. The optimal concentration of $Al_2(SO_4)_3\;and\;Ca(OH)_2$ was 480 ppm and 200 ppm, respectively. Optimal retention time of wastewater for $Al_2(SO_4)_3$ addition $Ca(OH)_2$ addition : flocculation was 2 : 2 : 10 min. Multiple treatment of $Al_2(SO_4)_3:Ca(OH)_2$ overcame coagulation inhibition by gelatin and detergent, and addition of microbial sludge reduced it.

• Proceedings of the Korean Institute of Resources Recycling Conference
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• 2004.05a
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• pp.53-58
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• 2004

동제련 공정중 고품질의 전기동을 효율적으로 생산하기 위해서는 Anode중에 적정량의 비소(As)가 필요하다. 그러나 Cu가 약30% 함유되어 있는 동정광에 함유된 비소는 Smelting Furnace 용련과정에서 비소 특성상 약 70%가 Offgas로 휘발되어 황산공장으로 유입 처리되고, 나머지 30%만 아노드(Anode)로 유입되므로 별도로 전련공정에서 발생된 Cu-Cement(비소 함유)를 정제로에 Recycle 하고 있으며, 부족시 추가로 비소 Source를 구입하여 정제로에 투입하고 있다. 이를 효과적으로 해결하기 위하여 현재 위탁처리를 하고있는 As가 함유된 폐수처리 2차 중화시 발생된 2차 Cake 60W.T/D중 30W.T/D를 기존 Converter Slag 건조용 Rotary Dryer를 이용하여 Converter Furnace에 Recycle 함으로써 전련 Anode에 필요한 비소를 공급하고, 또한 2차 Cake에 혼입되어 있는 CaO 활용으로 부재료 절감, 유가금속(Cu등) 회수등 및 2차 Cake 위탁처리비용을 절감하며, Cu-Cement는 Smelting Furnace에 투입하여 정제로 투입시 발생되는 문제점들을 동시에 해결코자 한다.

• KSBB Journal
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• v.8 no.2
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• pp.172-177
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• 1993

In order to reduce BOD of wastewater from alcohol distillery manufactory, the production of single cell lipid was attempted. Among five yeast strains tested, Rhodotorula glutinis was most desirable for lipid production. Wastewater was treated with 2N NaOH and used as a medium. The optimum pH and temperature for lipid production were found to be 5.0 and $30^{\circ}C$, respectively. The addition of monobasic phosphate was good for cultivation of Rhodotorula glutinis. The C/N ratio was an important factor for lipid production and composition. The best C/N ratio was 50 for the production of single cell lipid. By cultivation Rhodctorula glutinis for 4 days, 4g/L of single cell lipid was harvested and BOD of wastewater reduced by 88.7%.

• Korean Journal of Environmental Biology
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• v.20 no.3
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• pp.256-262
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• 2002

This research investigated experimentally on the population growth in the aquatic microcosm with the wastewater of plating factory. The purpose of this study was to evaluate the effect of culture conditions of the characteristic growth pattern of the examined species. Population of the system is consists of three organisms; Chlorella vulgaris as a producer, Cyclidium glaucoma as a consumer and Pseudomonas putida as a decomposer. The different growth patterns of each population are followed by surfactant type; Especially C. glaucoma was sensitive, Ch. uvlgaris was maintained population size stably even at high level of surfactant and p. putida was not significantly affected. After treatment of waste water from plating factory, it began to be affected at 1.0% solution treatment to Ch. vulgaris which the cell number was decreased prominently after 2 days, and C. glaucoma was disappeared at 2.5% solution treatment. P. putida was showed increasing pattern according to treatment concentration, at 2.5% solution and population size grew double. The result from current microcosm study indicates that this model system can be applied to environmental assessment method for various pollutants.

• Proceedings of the Korean Society for Applied Microbiology Conference
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• 1979.10a
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• pp.240.2-241
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• 1979

이태리의 Volta(1776)가 식물성 유기물을 혐기성으로 처리하면 메탄가스가 발생된다는 사실을 발견한 이래 많은 연구자들이 메탄가스에 관심을 가졌으며 1896년 영국의 Exeter에서는 분뇨의 메탄가스로 처음 가로등을 설치하였다. 그 후 메탄가스를 이용하기 위한 여러가지의 연구와 이용시설이 개발되어 양차 세계대전중에는 연료난에 직면한 독일, 영국 불란서의 농민들은 인축분뇨로 메탄가스를 생산하여 연료 및 전기, 자동차 및 트럭타의 연료로 사용하였고 특히 독일은 당시 유럽의 메탄가스연구의 중심지였다. 그러나 종전후에는 전후의 평화와 아랍국가들의 oil boom으로 대체에너지로서의 메탄가스이용 연구는 한때 관심이 적었으나 메탄발효(혐기성발효)는 에너지를 생산할 뿐만아니라 분뇨, 도시의 오수 및 공장폐수의 공해처리와 폐자원의 활용면에서 오늘날 메탄가스의 이용연구는 세계적으로 열을 올리고 있는 연구분야이다.