Kinetic Study of Treatment of Reactive Dye in a Biological Activated Carbon

碩士 === 中臺科技大學 === 安全與防災科技研究所 === 100 === Synthetic dyes were widely used in paper-printing, color photography, medicine and cosmetics etc. Approximately 90% reactive dyes flowed into receiving river from wastewater plant because the reactive dyes were not easy to be degraded by activated sludge. Con...

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Main Authors: Hsin-lung Li, 李欣龍
Other Authors: Yen-Hui Lin
Format: Others
Language:zh-TW
Published: 2012
Online Access:http://ndltd.ncl.edu.tw/handle/57329020796185769181
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spelling ndltd-TW-100CTC057070052017-04-29T04:31:06Z http://ndltd.ncl.edu.tw/handle/57329020796185769181 Kinetic Study of Treatment of Reactive Dye in a Biological Activated Carbon 生物活性碳處理反應性染料之動力研究 Hsin-lung Li 李欣龍 碩士 中臺科技大學 安全與防災科技研究所 100 Synthetic dyes were widely used in paper-printing, color photography, medicine and cosmetics etc. Approximately 90% reactive dyes flowed into receiving river from wastewater plant because the reactive dyes were not easy to be degraded by activated sludge. Conventional methods to deal with textile wastewater mainly included physical and chemical methods. Although, these methods were effective to treat textile wastewater, these methods have some disadvantages such as high cost, high energy requirement, and easy to produce chemical waste sludge. In this study, biological activated carbon was used to treat reactive dye in continuous-flow reactor. The batch kinetic tests were conducted to determine the yield coefficient of dye-degrading (F. trogii) cells, which was equal to 0.204 mg cell/mg RO16. The maximum specific growth rate (mm) was 0.63 day-1. The maximum specific utilization rate (k) was 3.1 mg RO 16/mg cell-day. The half-saturation constant was 107.3 mg RO 16/L. The decay coefficient of F. trogii cells was 0.024 day-1. The diffusion coefficient of RO 16 in biofilm was 0.192 cm2/day. The liquid film mass transfer coefficient was 346.8 cm/day. The shear-loss coefficient of F. trogii cells was 0.253 day-1. A continuous-flow fixed-biofilm reactor using activated carbon as a supporting medium was conducted in the laboratory. The experimental results show that the pH was maintained at 7.3-8.4 and influent DO was maintained at 7.8-8.2 in the influent. The pH and DO in effluent was 5.0-6.7 and 5.0-6.6 mg/L, respectively. The effluent concentration of RO 16 was 0.01-0.02 mg/L while the influent concentration of RO 16 was maintained at 10 mg/L. Once the influent concentration of RO 16 increased to 50 mg/L, the removal efficiency was about 97-98%. Moreover, the removal efficiency reached at 97-98% when the influent concentration of RO 16 was maintained at 100 mg/L. Yen-Hui Lin 林燕輝 2012 學位論文 ; thesis 106 zh-TW
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description 碩士 === 中臺科技大學 === 安全與防災科技研究所 === 100 === Synthetic dyes were widely used in paper-printing, color photography, medicine and cosmetics etc. Approximately 90% reactive dyes flowed into receiving river from wastewater plant because the reactive dyes were not easy to be degraded by activated sludge. Conventional methods to deal with textile wastewater mainly included physical and chemical methods. Although, these methods were effective to treat textile wastewater, these methods have some disadvantages such as high cost, high energy requirement, and easy to produce chemical waste sludge. In this study, biological activated carbon was used to treat reactive dye in continuous-flow reactor. The batch kinetic tests were conducted to determine the yield coefficient of dye-degrading (F. trogii) cells, which was equal to 0.204 mg cell/mg RO16. The maximum specific growth rate (mm) was 0.63 day-1. The maximum specific utilization rate (k) was 3.1 mg RO 16/mg cell-day. The half-saturation constant was 107.3 mg RO 16/L. The decay coefficient of F. trogii cells was 0.024 day-1. The diffusion coefficient of RO 16 in biofilm was 0.192 cm2/day. The liquid film mass transfer coefficient was 346.8 cm/day. The shear-loss coefficient of F. trogii cells was 0.253 day-1. A continuous-flow fixed-biofilm reactor using activated carbon as a supporting medium was conducted in the laboratory. The experimental results show that the pH was maintained at 7.3-8.4 and influent DO was maintained at 7.8-8.2 in the influent. The pH and DO in effluent was 5.0-6.7 and 5.0-6.6 mg/L, respectively. The effluent concentration of RO 16 was 0.01-0.02 mg/L while the influent concentration of RO 16 was maintained at 10 mg/L. Once the influent concentration of RO 16 increased to 50 mg/L, the removal efficiency was about 97-98%. Moreover, the removal efficiency reached at 97-98% when the influent concentration of RO 16 was maintained at 100 mg/L.
author2 Yen-Hui Lin
author_facet Yen-Hui Lin
Hsin-lung Li
李欣龍
author Hsin-lung Li
李欣龍
spellingShingle Hsin-lung Li
李欣龍
Kinetic Study of Treatment of Reactive Dye in a Biological Activated Carbon
author_sort Hsin-lung Li
title Kinetic Study of Treatment of Reactive Dye in a Biological Activated Carbon
title_short Kinetic Study of Treatment of Reactive Dye in a Biological Activated Carbon
title_full Kinetic Study of Treatment of Reactive Dye in a Biological Activated Carbon
title_fullStr Kinetic Study of Treatment of Reactive Dye in a Biological Activated Carbon
title_full_unstemmed Kinetic Study of Treatment of Reactive Dye in a Biological Activated Carbon
title_sort kinetic study of treatment of reactive dye in a biological activated carbon
publishDate 2012
url http://ndltd.ncl.edu.tw/handle/57329020796185769181
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