• Title/Summary/Keyword: 발포성 폴리스티렌

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Development of BNR(Biological Nutrient Removal) Process Using Expanded Polystylene(EPS) Media (Expanded Polystylene(EPS) 여재를 이용한 BNR(Biological Nutrient Removal) 공정 개발)

  • Ryu, Hong-Duck;Min, Kyung-Kook;Lee, Jeong-Hun;Choi, Kyoung-Young;Lim, Heun-Eun;Kim, Chul-Hwan;Lee, Sang-Ill
    • Journal of Korean Society of Environmental Engineers
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    • v.28 no.1
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    • pp.1-6
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    • 2006
  • Biological nutrient removal(BNR) process used in this study, which was packed with EPS(expanded polystylene) media, has more many advantages in aspect of reducing hydraulic retention time(HRT) of the process and having less effect of temperature in the winter season than commercial process in the present. Bench-scale study was performed using domestic wastewater. In the results, it was observed that the T-N removal efficiencies in HRT 6 hr and HRT 4 hr were 55% and 51%, respectively, showing the small reduction (about 4%) of T-N removal efficiency according to shortening of HRT. In comparison of T-N removal characteristic in summer and winter seasons, it showed that T-N removal efficiencies in summer and winter seasons were 65% and 54%, respectively, showing the 11% lower T-N removal efficiency in winter season than in summer season due to deterioration of nitrification in winter season. In the studies of influent loading rate and C/N ratio, the process showed stable effluent quality under the condition of broad influent loading rate and C/N ratio. Therefore, it is anticipated that the developed process in this study could be applicable to small wastewater treatment plant in nutrient removal.

A Study on Pyrolysis of Styrene Dimer Fraction (SDF) (스티렌 이량체 유분의 열분해 연구)

  • Pei, Hai-Song;Kang, Yong;Cho, Deug-Hee;Choi, Myong-Jae;Lee, Sang-Bong
    • Applied Chemistry for Engineering
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    • v.17 no.3
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    • pp.321-326
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    • 2006
  • Thermal degradation of styrene dimer fraction (SDF, main compound: 47 wt% of 1,3-diphenylpropane), 5~15% of total products produced during decomposition of waste expanded polystyrene (WEPS) was investigated. Reaction condition of $360^{\circ}C$, and 152 kPa to 202 kPa was an optimum for high pressure degradation. Under this operating condition, the yield of oil was 73.8% and the selectivities to Ben, Tol, EB, SM, and AMS were 0.4, 30.9, 15.0, 19.6, and 4.2%, respectively. Non-catalytic fixed bed continuous degradation was conducted at reaction temperatures of $510{\sim}610^{\circ}C$ and contact time ranges of 2~24 min, where the yield was increased by increasing of reaction temperature and contact time. A $Cr_2O_3$ catalyst showed the highest activity and SM yield among acid, base, and redox catalysts. The conversion of 74.6% and the yield of Ben, Tol, EB, SM, and AMS were 0.4, 21.6, 9.7, 17.9, and 3.5%, respectively at $560^{\circ}C$ and contact time of 24 min. It is thought that styrene is converted to EB and other secondary products throughout the formation of diradicals of styrene.