• Title/Summary/Keyword: Sludge reuse

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New Technology Development for Production of Alternative Fuel Oil from Thermal Degradation of Plastic Waste (폐플라스틱의 열분해에 의한 대체 오일 생산의 신기술 개발)

  • Lee, Kyong-Hwan;Roh, Nam-Sun;Shin, Dae-Hyun
    • Proceedings of the Korean Institute of Resources Recycling Conference
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    • 2005.10a
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    • pp.34-46
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    • 2005
  • For treating a huge amount of plastic waste with the environment problem, pyrolysis of plastic waste into alternative fuel oil is one of important issue in recycling methods. This study was introduced over the trend of generation of plastic waste, pyrolysis technology in domestic and foreign countries, basic technology in pyrolysis process and new technology of pyrolysis developed in KIER (Korea Institute of Energy Research). The characteristics of process developed in KIER are the continuous loading treatment of mixed plastic waste with an automatic control system, the minimization of wax production by circulation pyrolysis system in non-catalytic reactor, the reuse of gas produced and the oil recovery from sludge generated in pyrolysis plant, which have greatly the advantage economically and environmetally. The experiment result data in 300 ton/yr pilot plant showed about 81 wt% liquid yield for 3 days continuous reaction time, and also the boiling point distribution of light oil (LO) and heavy oil (HO) produced in distillation tower was a little higher than that of commercial gasoline and diesel, respectively.

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Evaluation of Autoheated Thermophilic Aerobic Digestion Process for the Treatment of Pig Manure Wastewater (돈사폐수의 고온 호기성 소화공정 적용 타당성 평가)

  • Chung, Yoon-Jin;Cho, Jong-Bok;Lee, Jin-Yong;Lee, Jong-Hyoung
    • Journal of the Korea Organic Resources Recycling Association
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    • v.3 no.2
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    • pp.103-114
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    • 1995
  • Since autoheated thermophilic aerobic digestion (ATAD) process has various advantages for the treatment of high-strength organic wastewater, active research and field application has been applied in U.S.A. and Canada, recently and the interest in ATAD process has been elevated for treating high-strength organic wastewater efficiently in Korea. Therefore, various experiments were carried out to evaluate the feasibility of ATAD process for the treatment of pig manure wastewater. The results of this study showed possibility to reuse pig manure wastewater as wet fodder or liquid compost, since ATAD process led excellent stabilization on the basis of odor and putrefaction. However. digested sludge can not be provided as wet fodder to most of hog farms without changing dry feeder system into wet system and as liquid compost to hog farms not having their own grass land. Since the results showed that the increase of temperature in reactor was resulted not from energy by biological activity. but from mechanical mixing energy. the reactor investigated in this study was against the principle of ATAD process. Therefore. if pig manure wastewater treated by ATAD can not be utilized as wet fodder. it is not economical to adopt ATAD process only for the treatment of wastewater.

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Calcium Removal from Effluent of Electronics Wastewater Using Hydrodynamic Cavitation Technology (수리동력학적 캐비테이션을 이용한 전자폐수 처리수에 함유된 칼슘저감에 관한 연구)

  • Park, Jin-Young;Kim, Sun-Jip;Lee, Yong-Woo;Lee, Jae-Jin;Hwang, Kyu-Won;Lee, Won-Kwon
    • Journal of Korean Society of Environmental Engineers
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    • v.29 no.6
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    • pp.715-721
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    • 2007
  • Residual calcium concentration is high, in general, at the effluent of the fluoride removal process in the electronics industry manufacturing semiconductor and LCD. To increase the stability of the membrane process incorporated for reuse of wastewater, the residual calcium is required to be pre-removed. Hyperkinetic Vortex Crystallization(HVC) process was installed in the electronics industry manufecturing semi conductor as a pilot scale for accelerating calcification of calcium ion. Compared to the conventional soda ash method, the 31% higher calcium removal efficiency was achieved when HVC was applied at the same sodium carbonate dosage. In order to maintain the economic calcium removal target of 70% preset by manufacturer, the dosing concentration of the soda ash was 530 mg/L based on influent flowrate. The seed concentration in the reactor was one of the critical factors and should be maintained in the range of $800\sim1,200mg$ SS/L to maximize the calcium removal efficiency. The calcite production rate was 0.30 g SS/g $Na_2CO_3$ in the average. The economic HVC passing time of the mixture was in the range of $2\sim5$ times. Relatively, stable calcium concentration was maintained in the range of $30\sim72$ mg/L(average 49 mg/L) although the calcium concentration in the feed was severely fluctuated with $74\sim359$ mg/L(average 173 mg/L). The HVC process was characterized as environment-friendly technology reducing chemical dosage and chemical sludge production and minimizing maintenance cost.