• Proceedings of the Korean Society for Applied Microbiology Conference
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• 1979.10a
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• pp.236-238
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• 1979

자연계에 배출되는 유기물함유폐수는 Figl 에 나타난 바와 같이 미생물의 생태적변동에 의해 정화된다. (표 1참조)이 자연현상을 인공장치에 의해 효율좋게 정화시키는 연구를 20수년전부터 개시하여 Test plant 및 Pilot plant을 작제하여, 검토하여 현재는 Fig. 2.에 나타난 바와 같은 실용화 plant가 다수, 가동하게 되었다. Fig. 2의 flow pheet를 개약설명한다. 먼저 폐수원액은 vibrating filter를 통과시키므로서 고형물은 제거된다. 이 용액을 구기조(Aeration tank)에 투입하여, 맹렬히 통기하면서, 호기분해를 행한다. 1 일간, 포기후, 호기성균체를 포함한 용액을 다음의 광합성세균배양조에 이행시켜, 4 일간 체류시키므로서 광합성세균등을 증식시킨다. 그후 응집침전제를 첨가하여, 광합성세균등의 Bacterial mass는 회수된다. 그 상맥부는 최종적으로 포기되고, (동기, 한랭에 있어서는 산포여상 Contact oxidation tower를 통과시킨다.) 소량의 침전제을 분리한 후 방류한다, 광합성세균이용에 의한 수처리기술의 특징은 1) 농후유기폐수를 희석하지 않고 정화처리할 수 있다. 2) 표3에 나타난 바와같이 적용할 수 있는 폐수의 종류는 많다. 3) 부산물로서 회수한 균체는 축산사료나 수산사료로서 이용할 수 있다. 표4 및 표5는 산난계 및 부화직후의 치어의 첨가사료 로서 이용한 일예이다.

• Proceedings of the Membrane Society of Korea Conference
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• 1998.04a
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• pp.87-88
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• 1998

1. 서론 : 반도체 제조공정중의 공정폐수로 발생되는 Si 미립자 함유폐수는 많은 양의 초순수와 1차세정 폐수로 방류되므로 유가물인 Si가 상당량 함유되어 있다. 이러한 폐수의 재이용을 위해 본 연구에서는 미립자 Si를 농축, 회수하고 양질의 처리수를 얻고자 한외여과막 분리공정을 적용하였고, 한외여과막 공정의 조업변수를 평가하여 air back flushing에 의한 막세척 효율 및 fouling 제어특성, 각각의 membrane이 갖는 분획분자량 특성에 따른 처리수 수질 및 flux 비교를 통해 scale up할 경우 필요한 조업변수를 얻고자 실시하였다.

• Proceedings of the Membrane Society of Korea Conference
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• 1997.10a
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• pp.105-106
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• 1997

1. 서론 : 급속한 산업화에 따른 수자원 고갈과 계속되는 가뭄으로 인해 일부지역에서는 물부족 사태가 갈수록 심화되고 있다. 또한 정부에서는 폐수배출 허용 기준의 단계적 강화는 물론 수질총량규제를 실시하여 폐수방류량을 근본적으로 해결할 수 있는 기술이 요구되고 있는데 그 방안이 폐수를 처리하여 공업용수로 재이용함으로서 대체용수를 확보함과 동시에 폐수방류량을 줄여 공공수역의 오염부하량을 저감하는 것이다. (생략)

• Applied Biological Chemistry
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• v.45 no.1
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• pp.25-29
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• 2002

The kernel of wastewater treatment by activated sludge is elimination of organic substances and maintenance of well-flocculated sludge sedimentation. By the conventional activated sludge treatment, the optimum F/M ratio of soybean wastewater treatment was 0.24 (kg-BOD/kg-MLVSS day) and sludge bulking was generated at 0.48 (kg-BOD/kg-MLVSS day). To improve the treatment capacity and operation quality in higher loading of soybean wastewater, influent pH was constantly controlled by 9.0 using NaOH as a coagulant agent. In this process, higher loading up to 2.88 (kg-BOD/kg-MLVSS day) was possible and SVI was maintained under 150 without bulking. This was equivalent to 7.2 times higher than maximum permissible load of the conventional activated sludge process.

• Journal of the Korean institute of surface engineering
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• v.12 no.2
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• pp.123-128
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• 1979

本교는 原調査報文 Plating and Surface Finishing;Recovery Pay! Vol 66. No2. (1979) 45~48P을 번역한 것으로 도금폐수의 회수재생에 드는 비용과 장치비 그리고 미국에 있어서의 도금공장의 폐수 회수처리 현황을 알아보는데 참고가 되리라 믿는다.(역자주) Plating and Surface Finishing지의 조사결과는 폐액회수장치를 설치한 도금공장회사들이 화공약품을 절약할 수 있었고, 공장폐수 내에 중금속 함유량의 한계치를 넘지 않도록 하는데 화학처리 비용을 들이지 않거나 최소한 줄일 수 있었다는 사실을 나타내 주고 있다.

• Journal of the Korea Organic Resources Recycling Association
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• v.14 no.4
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• pp.113-120
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• 2006

Wastewater generated through the food waste recycling process have known high concentration, BOD 20,000~150,000 mg/L, which has to treat to the proper level because of a ban on reclamation. But it is impossible to treat less than 10 days by existing water treatment plant. Ecodays Ltd. is to treat this wastewater during 2~4 days by ER-1, which can simultaneously induce the modified PFR(Plug Flow Reactor) of the oxygen transfer rate, MLVSS concentration, and influent concentration to top from bottom of reactor. We tested the pilot test about low concentration food wastewater(BOD 16,500 mg/L) and high concentration food wastewater(64,431 mg/L) at the food waste recycling plant of H-Gun(20t/d). Hydraulic retention time(HRT) of ER-1 for low concentration food wastewater is 2.5day. In low concentration conditions, ER-1 treatment efficiency is to appear BOD 99%, COD 98%, TN 97%, and TP 96%. While ER-1 process for high concentration food wastewater treatment is composed 2 stages, which are to be HRT 2.5day for law wastewater and HRT 1.5 day for secondary treatment. In high concentration conditions, ER-1 treatment efficiency is to appear BOD 97%, COD 84%, TN 66%, and TP 95%. It is treated without temperature control about high temperature($50^{\circ}C$) to appear low treatment efficiency in high concentration conditions.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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• v.4 no.2
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• pp.179-186
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• 2006

Chemical wastes are generated from nuclear facilities and R&D laboratories, but the uranium concentration in the final dried cake is evaluated into 11.2 Bq/g, which exceeds the exemption level of 10 Bq/g for each U isotopes, so the cake is categorized into a radioactive waste. Acid dissolution was applied to extract uranium from the waste sludge, and uranium adsorption on the dissolved solution was experimented by using IRN-77 and Diphosil bead. A large amount of resin was required to get above 80% of uranium removal, which was found to be due to a large amount of metal ions simultaneously dissolved from the precipitates with uranium. As an alternative method, acid dissolution is applied to the dewatered wet cake of the sludge, and the natural evaporation method is adopted for the dissolved solution. The uranium concentration of the dissolved solution was estimated to be 6.97E-01 Bq/ml, and the specific activity of the final waste sheets is evaluated to be 4.3 Bq/g. These results lead to the suggestion that the application of acid dissolution to the wet cake and the natural evaporation for the dissolved solution is an effective treatment method for chemical wastes containing uranium.

• Journal of Korean Society of Environmental Engineers
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• v.33 no.11
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• pp.855-859
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• 2011

The main pollutants from zirconium alloy tubing manufacturing process in nuclear industry are nitrate ($NO_3-N$) and fluoride (F-)Nitric acid, and hydrofluoric acid is used for acid pickling. The process for the removal of nitrate and fluoride is composed of 1st chemical coagulation, SOD (Sulfur Oxidation Denitrification) process using sulfur-oxidizing denitrification, and 2nd chemical coagulation. The characteristic of the wastewater treatment is an application of SOD process. The SOD Process is highly received attention because it is significantly different from existing processes for sulfur denitrification. A JSC (JeonTech-Sulfur- Calcium) Pellet is unification of sulfur and alkalinity material. According to result of SOD process in wastewater treatment plant, the removal efficiency of T-N was over 91% and the average concentration of T-N from influent was 147.55 mg T-N/L and that from effluent was 12.72 mg T-N/L. Therefore, SOD process is a useful to remove nitrogen from inorganic industrial wastewater and a new development of microbial activator was shown to be stable for activation of autotrophic bacteria.

• Korean Journal of Microbiology
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• v.35 no.3
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• pp.237-241
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• 1999

Phenolic resin wastewater contained 41,000 mglI phenol, 2,800 mg/l fonualdehyde and various chlorinated phenolic compounds. Candida tropicalis PW-51 isolated [rom the natural enVlfooment was able to degrade 1,000 mg/l phenol in the presence of 100 mglI formaldehyde, but it took much time to degrade phenol with the increase of formaldehyde in phenolic resin wastewater. %en the phenolic resin wastewater was diluted to 1/40, the initial concentration of phenolic compounds (phenols) was 882 mglI and degraded to 81 mglI by C tfVpicalis PW-51 in batch culture. In a continuous biological treatment, the phenolic resin wastewater was diluted to 40 (745 mglI), 20 (1,356 mglI), or 10 (2,875 mglI) times. The removal efficiency of phenols in 1/40- and lI20-diluted phenolic resin wastewater was about 92%, but the phenols in 1!1O-diluted wastewater were not degraded. The remained phenols in wastewater were absorbed by a mixture of activated carbon and rice bran (1:1, v:v) in the process of absorption which was connected to the biological treatment. The total removal efficiency of phenols in 1!40~ and l/20-diluted phenolic resin wastewater was 99.9%.

• Membrane Journal
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• v.32 no.2
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• pp.100-108
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• 2022

Among various industries, the textile industry uses the largest amount of water for coloring textiles which leads to a large amount of wastewater containing various kinds of dye. There are various methods for the removal of dye such as flocculation, ozone treatment, adsorption, etc. But these processes are not much successful due to the issue of recycling which enhances the cost. Alternatively, the membrane separation process for the treatment of dye in wastewater is already documented as the best available technique. Polymeric membrane and ceramic membrane are two separate groups of separation membranes. Advantages of ceramic membranes include the ease of cleaning, long lifetime, good chemical and thermal resistance, and mechanical stability. Ceramic membranes can be prepared from various sources and natural materials like clay, zeolite, and fly ash are very cheap and easily available. In this review separation of wastewater is classified into mainly three groups: ultrafiltration (UF), microfiltration (MF), and nanofiltration (NF) process.