• Title/Summary/Keyword: 저농도폐수

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Biological treatment process for Food wastewater Using ER-1 bioreactor (다단 수직형 호기성반응기(ER-1)를 이용한 음식물 폐수의 생물학적 처리기술)

  • Lee, Jae-ki;Choi, Hong-Bok;Shin, Eung-Bai;Park, Ju-Hyoung;Choi, Eun-Ju;Kim, Jung-Rae;Park, Young-Sook
    • 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.

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Development of Biological Denitrification Process using Sulfur for the Wastewater Containing Low BOD (저농도 BOD함유 폐수의 황(S)을 이용한 생물학적 탈질공정 개발 (SPAD 공정))

  • 광주과학기술원, 한국과학기술원;한국과학기술원;동명산업
    • Environmental engineer
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    • v.19 s.186
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    • pp.66-73
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    • 2002
  • 우리나라 하수의 특성이 유기물 농도가 질소 농도에 비하여 매우 낮기 때문에 외국의 종속영양 탈질 공법을 그대로 적용하기가 힘들며 적용한다 할지라도 외부탄소원을 넣어야 하므로 경제적인 처리는 불가능하다. 산업폐수의 경우에 있어서도 유기물농도가 질소농도에 비하여 낮은 폐수의 경우는 값비싼 외부탄소원을 넣어주어야 한다. 따라서 폐수 특성에 맞는 효율적이고 경제적인 질소화합물 제거 기술의 개발은 불가피하다. 따라서 종속영양탈질공정의 경제성 문제 및 기존의 황탈

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Development of Biological Denitrification Process Using Sulfur for the Wastewater Containing Low BOD (저농도 BOD함유 폐수의 황(S)을 이용한 생물학적 탈질공정 개발 (SPAD 공정))

  • 김인수;오상은;범민수;이성택;이창수;김민수
    • Environmental engineer
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    • s.183
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    • pp.70-77
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    • 2001
  • 우리나라 하수의 특성이 유기물 농도가 질소농도에 비하여 매우 낮기 때문에 외국의 종속영양 탈질 공법을 그대로 적용하기가 힘들며 적용한다 할지라도 외부탄소원을 넣어야 하므로 경제적인 처리는 불가능하다. 산업폐수의 경우에 있어서도 유기물농도가 질소농도에 비하여 낮은 폐수의 경우는 값비싼 외부탄소원을 넣어주어야 한다. 따라서 폐수 특성에 맞는 효율적이고 경제적인 질소 화합물 제거 기술의 개발은 불가피하다. 따라서 종속영양탈질공정의 경제성 문제 및 기존의 황탈

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A Study on the Removal of Low-concentration Fluoride-ion by Modified Alumina (변형 알루미나를 이용한 저농도 불소이온 제거 연구)

  • Kim, So-Young;Kim, Ju-Hee;Kim, Hyoun-Ja;Cho, Young-Sang
    • Journal of Korean Society of Environmental Engineers
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    • v.27 no.3
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    • pp.247-252
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    • 2005
  • The typical treatment method for fluoride polluted water is the flocculation and precipitation method which usually is capable of reducing the fluoride concentration down to the level of about 10 ppm. However, this method is no longer effective for the treatment of contaminated water having less than 10 ppm of fluorides. To remove fluorides in polluted water from the fluoride concentration between 1 to 10 ppm, several adsorbents were prepared mainly based on an activated alumina and the fluoride removal efficiencies of the adsorbents were analyzed. The best fluoride removal efficiency was obtained when the activated alumina treated by sulfuric acid was used as the adsorbent. A proper calcination temperature for the sulfuric acid contained activated alumina was found to be about $500^{\circ}C$. An adsorption isotherm for the adsorbent was also obtained by using Freundlich model. The values of the constants in Freundlich isotherm model were calculated to be K=6.63 and 1/n=0.29 based on the results obtained from the series of batch type adsorption experiments.

Growth Responses of Crops to Wastes Derived from Some Factories (수종 공장 폐수에 대한 작물의 피해 반응)

  • Kang, Byeung-Hoa;Shim, Sang-In;Lee, Sang-Gak
    • Korean Journal of Environmental Agriculture
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    • v.16 no.2
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    • pp.161-165
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    • 1997
  • This experiment were carried out to clarify the effects of several factory wastes on the emergence and seedling growth of five crop species, rice, Chinese cabbage, melon, and tomato. Wastes of three factories treated by several concentrations on the soil in which crop were seeded. In rice seedling experiments, the rice seedlings were treated with factory wastes hydroponically. Factory wastes used in the experiment were obtained from leather, phenol resin, and dye factory. The growth of rice seedlings was inhibited by each factory wastes, but the dry weight of rice seedling was increased by the low concentration below 1/16 dilution of leather factory waste. During 15 days, dry matter accumulation of rice seedlings treated with undiluted factory wastes decreased to 46.0, 51.4, -5.4% of control by treating wastes of phenol resin, leather, and dye factory respectively. The injury of crops by leather factory waste was severe in tomato but slight in barley. Waste of phenol resin factory affects highly both on Chinese cabbage and on melon. When dye factory waste was treated on each crop, all plants died in the treatments of waste solution which diluted to 1/8 of original waste. Tomato and melon were most sensitive crop species to the waste of dye factory. Although the responses of crops to each factory waste were various, the degree of injuries were more higher in vegetables than cereal crops.

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Development of the Biological Oxidation Filter System for Water Treatment (수처리용 생물산화 여과장치 개발)

  • 염병호;정충혁;문정석;최승일
    • Environmental engineer
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    • s.181
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    • pp.70-75
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    • 2001
  • 본 연구는 '99년 7월에 벤처형 중소기업 기술개발 지원사업으로 신규 계약된 과제로서 상수원수의 전처리 및 하수 2차 침전수의 재처리 공정에 활용될 생물 산화 여과지를 개발하는 것이다. 생물 산화 여과 system은 상수 원수의 전처리, 상수도의 고도정수 처리, 하수 및 폐수처리에 이용될 수 있는 것으로, 특히 물리적 여과기능과 포기 과정을 통한 산화 기능을 포함하는 생물학적 분해 및 자연정화처리환경을 유지하여 수질이 악화된 상수도의 전·후처리나 하.폐수의 3차 처리에 적용하기 위한 것이다. 생물 산화 여과 시스템은 여과지의 하부 장치에 균등한 공기(산소)공급시설을 하여 여과층에 연속적으로 공기를 공급하면서 여과를 함으로서 생물막 여과 및 산화 기능으로 유기물질, 철, 망간 등을 제거하고 공기의 부상력에 의하여 조류, 부유물질, 냄새 등을 동시에 제거하는 System이다. 현재 상수처리 공정으로서의 생물 산화 여과지 개발을 위해 Bench-scale과 semi-pilot plant를 거쳐 Y시 M취수장애 pilot plant를 설치하여 연구를 진행중에 있으며, 또한, G시 G하수처리장에 하수처리 공정에 관한 연구를 위해 pilot plant를 설치하고 하수 3차 처리와 저농도 하·폐수 처리를 중심으로 연구중에 있다. 아래의 연구 결과는 정수처리 공정 연구를 위한 Bench-scale plant실험을 통해 얻은 결과치이며 현재까지 진행된 연구는 주로 정수처리 공정 중심으로 이루어 졌으나 pilot plant에서는 정수 및 하수처리에서의 생물산화여과공정의 연구가 진행중이다. 현재 연구가 진행중이므로 각 인자별 최적운전조건 등은 계속적인 실험과 연구를 통해 찾아지겠으나 현재까지 수행된 연구자료를 기반으로 볼 때 생물산화 여과장치는 탁도, SS, VSS 등의 제거에 탁월한 효능을 보이고 있다. 수처리용 장치로서의 이러한 기본적인 기능 이외에 NPOC, DOC 제거에도 뛰어난 효능을 보이고 있으며 특히 정수처리 공정에서 문제시 되고 있는 동절기 암모니아성 질소제거 또한 큰 가능성을 보여주고 있다. 그 동안 외국기술에 전면 의존해 오던 생물 산화 여과방식의 국내개발은 비용 절감뿐만 아니라 국내 실정에 맞는 기술개발이라는 점에서 향후 그 적용 범위를 넓혀 갈 수 있을 것이다.

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Development of Polymeric Adsorbents for the Treatment of Coloured Waste Waters and it's Application (I) - Carboxymethylated Cellulosic Adsorbent System - (유색폐수처리를 위한 고분자흡착제의 개발과 처리수의 재사용(I) - Carboxymethyl화 셀룰로오스흡착제 -)

  • Soo Min Park
    • Textile Coloration and Finishing
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    • v.4 no.2
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    • pp.84-88
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    • 1992
  • 셀룰로오스 펄프에 폴리비닐알코올의 블랜드, 가교, 및 카복시메칠화한 아니온성 셀룰로오스계 고분자 흡착제에 대한 모델 카치온 염료, C.I. Basic Red 18의 흡착 및 탈색 성능을 수용액계(pH 4.2)에서 검토하였다. 아니온성 셀룰로오스 고분자 흡착제의 카치온 모델 염료의 흡착등온성은 저농도 영역에서 Sigmoidal 형을 나타내었고 Donnan 흡착 모델 기구로 해석하였다. 하전기 도입에 따라 염료의 흡착능은 증가하였으며 이 흡착능력은 Sodium이온의 첨가에 의하여 저하하였다. 또 아니온 셀룰로오스계 흡착제에 의한 모델 염료의 배수 탈색율은 크게 증가하였으며 입상활성탄보다 우수한 탈색능력을 나타내었다.

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Temperature Effects on Type and Concentration of Substrate in Activated Sludge Process (활성(活性)슬러지공법(工法)에 있어서 유기물(有機物)의 성상(性狀)과 농도(濃度)에 따른 온도영향(溫度影響))

  • Choi, Eui So;Min, Kyung Sok
    • KSCE Journal of Civil and Environmental Engineering Research
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    • v.5 no.4
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    • pp.45-56
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    • 1985
  • This study was made to evaluate temperature effects on biological wastewater treatment particularly at the lower temperatures. Cell yield coefficients and other kinetic factors were compared by varying temperature for industrial wastes. Bench scale aeration-only complete mixing activated sludge(CMAS) units were operated at temperatures of $1^{\circ}$, $4^{\circ}$, $7^{\circ}$ and $10^{\circ}C$ with substrate concentrations of 5,000 and 200 mg/l COD. The study results indicate that the cell yields were computed to be 0.5 to 0.6 grams VSS per grams BOD removed, and were not influenced by temperature variations. The synthesis/total energy ratios were computed to be 0.45 to 0.58 and had a tendency to become larger at lower temperatures. The endogenous respiration rates were computed to be 0.07 to 0.08/day, and seemed to be independent of temperature. In addition, very little temperature effects were observed when F/M ratio and substrate concentrations were reduced.

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Extraction of nitrate salts from de-NOx waste scrubbing solution (탈질 스크러버의 폐세정액으로부터 질산염 추출 연구)

  • Kim, Wooram;Ha, Taeyoung;Park, Yeonsoo;Lee, Hyunsuk;Jo, Youngmin
    • Journal of the Korean Applied Science and Technology
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    • v.34 no.2
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    • pp.210-216
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    • 2017
  • Recovery of low level nitric acid and sulfuric acid ions, which were contained in wastewater of a wet scrubber for de-NOx and de-SOx from ship engines, was attempted as fertilizing materials. This study utilized a selective extraction method using four organic solvents to precipitate the solid salts of ammonium nitrate and ammonium sulfate. The IR analysis showed almost same composition of the extracted ammonium salts with a commercial product, and recovery rate of nitrogen and sulfuric ions was 89% and 80% respectively. It was found that the selectivity and solubility consequently could be the crucial factors to recover the low level ions from the waste scrubbing water.

Principle and Application of Biofiltration (바이오필터 기술의 원리와 적용에 관한 고찰)

  • Namkoong, Wan;Park, Joon-Seok;Lee, Noh-Sup
    • Journal of the Korea Organic Resources Recycling Association
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    • v.8 no.1
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    • pp.60-68
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    • 2000
  • Biofiltration is an environmentally-sound technology for elimination of VOCs and odorous compound from low-concentration, high-volume waste gas streams because of its simplicity and cost-effectiveness. It can be appled to the treatment of gases from publicly owned treatment works, composting facilities, landfill sites, and soil vapor extraction systems. The ability to design an effective biofilter system involves a combination of fundamental biofilter knowledge, practical experience, and bench- and pilot-scale testing. The objective of this paper was to review principle, design parameters, operational conditions, case studies, and economy of biofiltration through literature.

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