• Title/Summary/Keyword: 폐수슬러지

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Analysis and Distribution of Polycyclic Aromatic Hydrocarbons and Chlorophenols in Sewage and Industrial Wastewater Sludge in Korea (국내 하.폐수슬러지 중 다환방향족탄화수소 및 염화페놀류의 분포 특성)

  • Ju, Joon-Hyung;Kim, Min-Young;Lee, Sung-Hee;Oh, Jeong-Eun
    • Journal of Korean Society of Environmental Engineers
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    • v.30 no.7
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    • pp.735-742
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    • 2008
  • In order to evaluate the levels and distribution patterns, the concentrations of PAHs and chlorophenols were investigated in sludge samples discharged from 6 WWTPs located along Nak-dong river and 7 STPs in Busan, Korea. Levels of 16 PAHs and 19 chlorophenols in sludge samples ranged from 1.28 to 44.9 mg/kg dry wt. and from 213 to 3,850 $\mu$g/kg dry wt., respectively. Levels of PAHs in sludge samples except I5 and S4 were detected lower than those of previous studies. The distribution patterns of PAHs and chlorophenols varied with industrial wastewater sludge samples because industrial wastewater sludge had different industrial input sources. However, the distribution patterns of PAHs and chlorophenols in sewage sludge were pretty similar. Phenanthrene, fluoranthene and pyrene were dominant and the fractions of these 3 PAHs relative to 16 PAHs in sewage sludge ranged from 30.8 to 50.7%. 2-chlorophenol is dominated in most sewage sludge samples and the fraction ranged from 36.0 to 66.8%.

Disintegration of Waste Activated Sludge by Acid Hydrolysis (산 가수분해에 의한 폐활성슬러지 분해)

  • Patchareeya Jaipakdee;Yeonghee Ahn
    • Journal of Life Science
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    • v.33 no.1
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    • pp.82-90
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    • 2023
  • Biological process is used worldwide to treat domestic and industrial wastewater. The process generally uses a mixed microbial culture of sludge. The growth of microorganisms in the sludge produces excess sludge from the wastewater treatment process. Some of the excess sludge is recycled as inoculum for wastewater treatment, but the rest is removed as waste from the process. As wastewater production is increasing worldwide every year, the number of wastewater treatment plants (WWTPs) is also in- creasing, resulting in the generation of large amount of waste sludge. The increasing amount of waste sludge from WWTPs has led to concerns about its management. Sludge disposal has been reported to account for 50~60% of the total operating costs of a WWTP. Sludge disintegration is a new technology that can minimize volume of waste sludge and recover useful components (e.g., P, N, and soluble organic compounds) from it. Various methods of sludge disintegration have been developed based on physical, chemical, and biological treatments or combinations of these. In this review, we focus on sludge disintegration by acid hydrolysis, which is less studied among sludge disintegration methods. Such information can be useful in the development and implementation of a new technology for better sludge treatment.

Soybean Wastewater Treatment by Activated Sludge Process (고농도 대두가공폐수의 처리를 위한 개선 활성슬러지법)

  • Cho, Kwon-Ik;Lee, Jeoung-Su;Lee, Tae-Kyoo;Kim, Jong-Hwa
    • 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.

A kinetic study of steam gasification of sewage sludge (하수슬러지 촤의 수증기 가스화반응특성)

  • 장용원;송병호
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 2002.05a
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    • pp.239-244
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    • 2002
  • 하수슬러지는 산업의 발달 및 인구의 증가로 인하여 증가하는 폐수의 양에 비례하여 증가하고 있다. 폐수 처리량과 함께 슬러지의 발생량은 1997년 이후 매년 3% 이상의 증가를 보이고 있다. 특히 최근에는 수질환경 개선 사업의 확대로 인하여 하수처리장이나 폐수처리장의 처리 용량은 매련 증가하고 있으며, 농축산 산업의 발달로 농촌지역의 농수산 폐수처리장의 시설용량의 증가로 슬러지 발생량 증가는 가속되어 2005년에는 연간 1000만톤 이상이 발생할 것으로 예측되고 있다.(중략)

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A Study on the sludge drying using waste heat of cogeneration plant (열병합발전소 보일러 폐열을 이용한 슬러지 건조 연구)

  • Ryu, Seung-Han;Lee, Sang-Hun;Shin, Dong-Hoon;Park, Jun-Hyung;Jo, Suk-Jin;Kwak, Sung-Sik;Woo, Young-Hoon;Jeon, Jong-Seok
    • Proceedings of the Korean Society of Dyers and Finishers Conference
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    • 2011.11a
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    • pp.60-60
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    • 2011
  • 염색폐수의 정화에는 필연적으로 다량의 슬러지 폐기물이 발생한다. 염색폐수 슬러지는 그간 인근 공해 해상에 투기하는 해양 배출로 저렴하게 처리하였으나, 해양오염을 우려하는 국제협약(1972년 런던협약, 1996년 교토의정서)에 의하여 2008년 8월부터 배출기준이 강화되고 2012년 2월부터는 해양배출이 금지 될 예정이다. 염색폐수 슬러지의 해양 배출이 금지되면 대체 처리방법으로는 지정매립장을 통한 매립처리 방법이나 고온 소각시설에서의 소각처리 방법이 거론되고 있다. 그러나 매립처리는 슬러지 내 함유 수분으로 인한 침출수의 문제와 더불어 장기간 안정적으로 저렴하게 사용할 수 있는 대규모 처분장을 확보하기 어려운 실정이며 소각처리는 슬러지의 높은 함수율로 인해 소각 시보조 연료의 투입이 필연적으로 최근 원유가 급등 등 에너지 비용이 지속적으로 상승함을 고려할 때 소각처리비용 또한 상당한 고가가 될 것으로 예측된다. 이와 같이 슬러지 해양배출이 금지되면 섬유 염색업체들은 많은 환경비용 부담을 안을 것이다. 본 연구에서는 대규모 염색산업단지 공동폐수처리장에서 발생하는 염색폐수 슬러지의 효율적인 건조를 위해 산업단지 내의 열병합발전소에서 발생하는 보일러 폐열을 이용하였으며, 조건 특성 및 효율을 파악하기 위해 보일러 폐열의 특성을 고려하여 슬러지 두께 및 체류시간 등 건조공정 운영조건에 따른 변수별 연구를 수행하였다. 열병합발전소 보일러에서 배출되는 폐열은 온도가 $150^{\circ}C$ 정도로 기존의 슬러지 건조에서는 사용되는 $700^{\circ}C$에 비해서는 매우 저온이다. 하지만 보일러 배가스의 경우, 온도에 비해 많은 풍량을 가지고 있으므로 열량으로 환산시 충분히 가치가 있는 것으로 조사되었다. 염색폐수 슬러지의 경우, 함수율 70% 이내의 탈수 Cake 형태이므로 두께가 두꺼울수록 건조효율이 감소하였으며, 체류시간이 길어질수록 건조효율은 증가하나 20mm 이상에서는 건조효율이 급격히감소하였다. 이를 바탕으로 5톤/일 규모 슬러지 건조 Pilot Plant를 제작하여 운영하였는데, 염색폐수슬러지의 투입공정에서 슬러지와 열풍의 접촉면적을 넓혀 건조효율을 높이기 위하여 슬러지를 압출노즐을 이용하여 슬라이스 칩 형태로 제조하여 건조공정에 투입하였으며, 건조실 내에서도 건조효율의 상승을 위하여 내부열풍순환팬을 설치하여 운영하였다. Pilot 운영결과, 체류시간 52분에서 슬러지의 함수율은 70%에서 10%이하로 감소하였다.

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A Study on Drying and Carbonization of Organic Sludge from Sewage Plant and Petrochemical Industries for Energy and Resources Recovery (하수슬러지 및 석유화학산업단지 폐수슬러지의 에너지화와 재활용을 위한 건조 및 탄화에 관한 연구)

  • Jun, Kwan-Soo;Hwang, Eung-Ju;Kim, Hyung-Jin
    • Clean Technology
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    • v.15 no.3
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    • pp.154-164
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    • 2009
  • In 2007, 94% of organic wastewater sludge from industries located in Ulsan was disposed of by ocean dump. The ocean dump of organic sludge would be totally prohibited by the year of 2012. However, there is no alternative but incinerating the sludge from the industries located in Ulsan. Securing the technology for sludge treatment and on-land disposal is very important issue among the industries in the Ulsan Petrochemical Industry Complex. In this study, the material aspects of dried and carbonized sludge as a fuel were evaluated for petrochemical and sewage sludge from Ulsan. The dried and carbonized sludges from the factories producing terephthalic acid, BTX, propylene, chemical textile, etc. of which the low heat value exceeded 3,000 kcal/kg had high potential as a fuel according to the results of thermal characteristic analysis. However, the dried sludges with heat values lower than 2,100 kcal/kg and carbonized sludges, lower than 1,100 kcal/kg containing more Inorganic material from the industries producing pulp, paper, methylamine, amide, etc. had a little potential to be used as a fuel. In most cases, drying the sludge showed better results than carbonization in the aspect of thermal characteristics of sludge.

Sludge Disposal Analysis of Sanitary Paper Manufacturing Wastewater Treatment Plant (위생용지 생산 제지공장 폐수슬러지의 처리 현황)

  • Jung, Yong-Jun;Lee, Hong-Tae
    • 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.

The Effects of Fe-coagulants in Real Textile Wastewater Treatment Process (염색폐수처리 공정에서 Fe 성분 응집제의 효능)

  • Hong, Young-Ho
    • Proceedings of the KAIS Fall Conference
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    • 2009.12a
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    • pp.655-658
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    • 2009
  • 본 연구는 철 성분 응집제가 염색폐수 처리공정에서 슬러지 발생에 미치는 영향에 대한 연구로 응집제로 $FeCl_3$, $FeSO_4$, $Al_2(SO_4)_3$를 사용하였다. 본 연구의 목적은 염색폐수처리공정에서 발생되는 폐수를 응집제를 이용하여 처리할 때 부수적으로 발생되는 슬러지의 양을 감량하며, 응집제가 색도제거에 미치는 영향에 대한 상관성을 규명 하는데 그 목적이 있다. 실험에 사용된 염색폐수의 BOD, COD, pH, 그리고 색도의 평균값은 각각 800 mg/L, 600 mg/L, 9.7, 102 이었다.

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Convergence Study on Organic Sludge Treatment System (유기성 슬러지 처리 시스템에 관한 융합연구)

  • Han, Doo-Hee
    • Journal of the Korea Convergence Society
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    • v.11 no.10
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    • pp.213-217
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    • 2020
  • An eco-friendly water purifier was developed using natural minerals, plants, and sludge from water purification plants. A wastewater complex treatment system using this water purification agent was developed. The wastewater complex treatment system goes through the process of inflow of contaminated water, input of water purification agent, operation of a pressurized flotation device, sludge flotation, sludge collection and treatment water discharge. This device was applied to the removal of green algae in livestock desorption liquid, broiler washing water, factory wastewater, sewage treatment plant and pond to obtain excellent removal rate. The use of natural water purification agents for organic waste purification has not been investigated.