• 제목/요약/키워드: Odor removal

검색결과 232건 처리시간 0.027초

MEK 제거를 위한 바이오필터용 담체의 선택 (Selection of Biofilter Support for Removing MEK)

  • 정귀택;이광연;이경민;선우창신;이우태;정승호;차진명;장영선;박돈희
    • KSBB Journal
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    • 제21권1호
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    • pp.34-41
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    • 2006
  • 본 악취제거용 바이오필터에 필요한 담체에 대하여 실험한 결과 다음과 같은 결론을 얻었다. 합성악취가스의 조성이 MEK 250 ppm을 바이오필터에 통과시켰을 때, 폴리프로필렌 섬유상은 $586.6g-MEK/m^3\;hr$로 실험담체 중에서 최고 제거량을 나타내었다. 폴리우레탄 담체는 $359.7g-MEK/m^3\;hr$을 제거용량을 나타내었다. 화산석 담체의 제거량은 $56.2g-MEK/m^3\;hr$으로 평가되었다. 본 연구에서 사용한 담체 중에서 MEK 제거에 사용될 수 있는 최적의 담체로는 폴리플로필렌 섬유상 담체로 평가되었다.

Disposal of Animal Waste-The Magnitude of the Problem in Asia and Australasia - Review -

  • Sheen, S.Y.;Hong, C.M.
    • Asian-Australasian Journal of Animal Sciences
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    • 제12권4호
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    • pp.597-603
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    • 1999
  • Even though the development of livestock industry in Asia and Australasia has brought the economic growth and thus elevated the living standard in these areas, it has also brought the pollution caused by the increasing amount of animal wastes. Among them, Japan probably is the first country that suffered from the animal waste pollution as early as in 1970s. Nowadays, the animal waste pollution has been a common problem for almost every countries in this region. To solve it, different measures and regulations have been implemented in many countries. In this paper, different methods for animal waste disposal are discussed, including: manure-bed animal housing, composting, anaerobic treatment, odor control, utilization of biogas, aerobic treatment, three-step process, N and P removal, land application, cultivation of algae, anaerobic treatment of dead animals. It is hoped that an animal industry without pollution can be achieved in the future.

이.취미물질(IBMP, IPMP)의 흡착제거 (Adsorption Removal of Odor Compounds (IBMP, IPMP))

  • 김은호;손희정;김영웅
    • 환경위생공학
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    • 제14권2호
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    • pp.18-24
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    • 1999
  • The purpose of this study was carried out to estimate removal possibility of IBMP and IPMP causing odor in raw water. As a result of Freundlich isotherm. IBMP was superior to IPMP in adsorptive capacity. Adsorptive capacities of activated carbon were found to be in order of Lignite, Coconut shell, and Charcoal. These were well fitted with Freundlich isotherm. According to adsorption breakthrough tests for Lignite GAC, breakthrough time of IPMP and IBMP were 5.7hr and 5.5hr, respectively. Because adsorptive capacities of target material were very different with pore size distribution, it seemed that Lignite and Coconut shell based activated carbons were recommended in order to remove door compounds.

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의류 중의 미생물에 대한 소비자의 지식과 세탁습관 실태조사 분석 (Analysis of the Survey on the Consumer's Knowledge and Laundry Habits to Microorganisms Living in Clothing)

  • 최해운;정찬진;박명자
    • 복식문화연구
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    • 제10권6호
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    • pp.781-792
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    • 2002
  • Microorganisms living in clothing cause damage to fabric as well as unhygienic conditions with unpleasant odor fur wearers. Removal or growth of microorganisms are affected by the conditions during washing and storage. The purpose of this research was to study the consumer's knowledge and habits in laundering with respect to microorganisms in clothing. For survey method, questionnaires were administered to 580 housewives, age of 20∼60s living in Seoul. Employing 479 respondents, the data were analyzed by using descriptive statistics. The results are as follows: The level of knowledge about microorganisms of clothing was high in general, but wasn't expert level. Many people had experienced damages of textiles, clothing and unpleasant odor due to microorganisms. Fabric softeners and bleaches were rarely used for disinfection but usually used for antistatic, whitening or removal of stains. There was no relationship between laundering habits, the knowledge of microorganism, and experience of clothing damage by microorganism.

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부산수영하수처리장 하수와 음식물쓰레기 병합처리 시 공정별 악취특성 및 후처리시설 효율평가 (Removal Efficiency of the Deodorization Equipment and Characteristics of Malodor during the Process in Co-treatment of Sewage and Food Waste of Su-young Wastewater Treatment Plant in Busan)

  • 이형돈;강대종;이민호;강동효;오광중
    • 청정기술
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    • 제18권4호
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    • pp.379-389
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    • 2012
  • 우리나라는 소득증가, 도시집중화, 인구증가로 인해 환경적인 문제에 대해 점점 관심이 증대되고 있으며, 이러한 다양한 환경문제 중 악취로 인한 피해는 심각한 환경문제 중 하나이다. 부산시 수영하수처리장 내 음식물처리장은 음식물과 하수를 병합처리하는 시설로 주거지역 인근에 위치해 있어 많은 민원이 제기되고 있는 실정이다. 이에 본 연구에서는 악취물질분석과 기여도를 악취지수(odor quotient, OQ)와 총악취지수(sum of odor quotient, SOQ)를 평가하여 분석하였으며, 또한 후처리시설인 바이오필터의 효율을 평가하였다. 공기희석관능법에 의한 복합악취 측정결과, 7월과 8월에 분쇄기, 투입호퍼, 침출수 순으로 복합악취가 높은 것으로 나타났다. 기기분석법을 이용해 분석한 결과, 황화수소, 암모니아, 메틸메르캅탄, 아세트알데히드에 의한 영향이 가장 큰 것으로 나타났고, 메틸메르캅탄의 경우, 최소감지농도를 3,571배 이상 초과한 것으로 나타났다. 또한 악취기여도평가에서 메틸메르캅탄(49.95~59.08%), 황화수소(20.43~29.27%), 트리메틸아민(8.82~13.42%), 아세트알데히드(9.17~11.35%)순으로 기여도가 높은 것으로 나타났다. 다른 시설과의 기여도를 비교분석한 결과, 황화합물(메틸메르캅탄, 황화수소)의 OQ가 가장 높았으며, 분쇄기에서 SOQ가 7,067로 가장 높은 것으로 분석되었다. 또한 황화합물과 아세트알데히드, 트리메틸아민의 악취기여도가 분쇄공정에서 가장 높은 것으로 나타났다. 본 연구시설의 후처리시설에 대한 처리효율을 평가한 결과, 암모니아, 아민류는 90.00% 이상의 처리효율을 보였으나, 황화합물류의 처리효율은 평균 53.51%로 나타났다. 종합적으로 본 시설은 기타 처리시설에 비해 아세트알데히드와 트리메틸아민의 기여도가 상대적으로 높은 것으로 나타났다. 또한 음식물처리장의 후처리시설은 복합적인 악취성분 처리 시 분해효율이 감소할 수 있어 적절한 용량 및 운전조건에 대한 검토가 필요하다.

악취물질인 유기산 제거를 위한 DBD 플라즈마 촉매 복합공정의 적용 (Application of DBD Plasma Catalysis Hybrid Process to remove Organic Acids in Odors)

  • 홍은기;서정민;최금찬
    • 한국환경과학회지
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    • 제23권9호
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    • pp.1627-1634
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    • 2014
  • Odor control technology include absorption, adsorption, incineration and biological treatments. But, most of processes have some problems such as secondary organic acids discharge at the final odor treatment facility. In order to solve the problems for effective treatment of organic acids in odor, it is necessary to develop a new type advanced odor control technology. Some of the technology are plasma only process and plasma hybrid process as key process of the advanced technology. In this study, odor removal performance was compared DBD(Dielectric Barrier Discharge)plasma process with PCHP(plasma catalysis hybrid process) by gaseous ammonia, formaldehyde and acetic acid. Plasma only process by acetic acid obtained higher treatment efficiency above 90%, and PCHP reached its efficiency up to 96%. Acetic acid is relatively easy pollutant to control its concentration other than sulfur and nitrogen odor compounds, because it has tendency to react with water quickly. To test of the performance of DBD plasma process by applied voltage, the tests were conducted to find the dependence of experimental conditions of the applied voltage at 13 kV and 15 kV separately. With an applied voltage at 15 kV, the treatment efficiency was achieved to more higher than 13 kV from 83% to 99% on ammonia, formaldehyde and acetic acid. It seems to the odor treatment efficiency depends on the applied voltage, temperature, humidity and chemical bonding of odors.

하수관거 악취 제거를 위한 맨홀필터 악취제거장치 성능 평가 - 황화수소 제거를 중심으로 - (Performance Evaluation of Manhole Filter to Remove Odor Inside Sewage Pipe -Focused on Removal of Hydrogen sulfide-)

  • 김충곤;이장훈
    • 유기물자원화
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    • 제26권4호
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    • pp.45-51
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    • 2018
  • 본 연구는 도심지 거리 하수 악취 물질인 황화수소($H_2S$)를 제거하기 위해 맨홀에 설치해 악취를 제거하는 맨홀필터 악취제거장치의 적용 가능성을 확인하고자 하였다. 첫번째로 맨홀필터에 들어 있는 첨착활성탄의 황화수소($H_2S$) 흡착 성능 평가 결과 황화수소 제거율이 약 99.8%를 나타냈다. 두 번째로 악취제거장치 성능평가를 위해 서울특별시 대표적인 악취 발생 맨홀 4지점에서 성능을 평가한 결과, 대표적인 악취 유발물질인 황화수소($H_2S$)를 97% 이상 제거하는 것으로 확인되었다. 본 성능 평가 연구결과를 통해 맨홀필터 악취제거장치는 하수관거 맨홀에서 발생되는 악취를 제거하는 장치로써 적용 가능성이 충분한 것으로 판단된다.

분말활성탄 접촉조의 맛·냄새 및 유기물 제거 효율 평가 (Performance Evaluation of Powdered Activated Carbon (PAC) Contactor for the Removal of Organics and Taste and Odor)

  • 배병욱;임문구
    • 한국물환경학회지
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    • 제26권4호
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    • pp.585-589
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    • 2010
  • In order to evaluate the performance of a powdered activated carbon (PAC) contactor, two water treatment plants (WTP) were selected as target sites. The result of tracer tests showed that the plug flow portion of a bisymmetry-type contactor (H WTP) was more than 70%. A maze-type contactor (C WTP) also had more than 70% of plug flow portion after intra-basin baffles were installed. According to the operating data of the target WTPs, there was no clear evidence that the addition of PAC contributed to the removal of organics. However, the results of jar tests, conducted with the raw water taken from the H WTP, proved that PAC could remove dissolved organic carbon (DOC) to some extent when the proper velocity gradient was maintained. It was estimated that the production rate, defined as the ratio of the operating flowrate to the design flowrate, of the C and H WTPs was only 27 and 50%, respectively. Because of these lower production rates, the mixing intensity in the contactor was much less than the designed value and, finally, the performance of the PAC contactor was much lower than what was expected.

상수원수 내 이취미 제거효율 향상을 위한 분말활성탄 투입지점의 평가 (Evaluation on the Locations of Powdered Activated Carbon Addition for Improvement of Taste and Odor Removal in Drinking Water Supplies)

  • 김영일;이상진;배병욱
    • 상하수도학회지
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    • 제21권3호
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    • pp.341-348
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    • 2007
  • The efficiency of powdered activated carbon (PAC) for removing taste and odor (T&O) in drinking water supplies is dependent on the contact time, quality of mixing, and the presence of competing compounds. All of these are strongly influenced by the stage in the treatment process at which the PAC is added. In conventional water treatment plants (WTPs), PAC is commonly added into the rapid mixing basin where chemicals such as coagulants, alkaline chemicals, and chlorine, are simultaneously applied. In order to prevent interference between PAC and other water treatment chemicals, alternative locations for addition of PAC, such as at transmission pipe in the water intake tower or into a separated PAC contactor, were investigated. Whatever the location, addition of PAC apart from other water treatment chemicals was more effective for geosmin removal than simultaneous addition. Among several combinations, the sequence 'chlorine-PAC-coagulant' produced the best result with respect to geosmin removal efficiency. Consequently, when PAC has to be applied to cope with T&O problems in conventional WTPs, it is very important to prevent interference with other water treatment chemicals, such as chlorine and coagulant. Adequate contact time should also be given for adsorption of the T&O compounds onto the PAC. To satisfy these conditions, installation of a separated PAC contactor would be the superior alternative if there is space available in the WTP. If necessary, PAC could be added at transmission pipe in the water intake tower and still provide some benefit for T&O treatment.