The implementation of data reconciliation for evaluating a full-scale petrochemical wastewater treatment plant

The implementation of data reconciliation for evaluating a full-scale petrochemical wastewater treatment plant


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صفحه نخست سامانه
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دانشگاه علوم پزشکی تبریز
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نویسندگان: محمد شاکرخطیبی , رضا دهقانزاده ریحانی

کلمات کلیدی: Performance evaluation . Wastewater . Petrochemical . Activated sludge . Data reconciliation

نشریه: 55141 , 2016 Aug 24 , 10.1007/s11356-016-7484-5 , 2016

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نویسنده ثبت کننده مقاله محمد شاکرخطیبی
مرحله جاری مقاله تایید نهایی
دانشکده/مرکز مربوطه دانشکده بهداشت
کد مقاله 58736
عنوان فارسی مقاله The implementation of data reconciliation for evaluating a full-scale petrochemical wastewater treatment plant
عنوان لاتین مقاله The implementation of data reconciliation for evaluating a full-scale petrochemical wastewater treatment plant
ناشر 6
آیا مقاله از طرح تحقیقاتی و یا منتورشیپ استخراج شده است؟ بلی
عنوان نشریه (خارج از لیست فوق)
نوع مقاله Original Article
نحوه ایندکس شدن مقاله ایندکس شده سطح یک – ISI - Web of Science
آدرس لینک مقاله/ همایش در شبکه اینترنت http://link.springer.com/article/10.1007/s11356-016-7484-5/fulltext.html

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Abstract Data reconciliation and mass balance analysis were conducted for the first time to improve the data obtained from a petrochemical wastewater treatment plant (WWTP), and the results were applied to evaluate the performance of the plant. Daily average values for 209 days from the inlet and outlet of the plant obtained from WWTP documentation center along with the results of four sampling runs in this work were used for data reconciliationandperformanceevaluationoftheplant.Resultsshowed that standard deviation and relative errors in the balanced data of eachmeasurementdecreased,especiallyfortheprocesswastewater from 24.5 to 8.6 % for flow and 24.5 to 1.5 % for chemical oxygen demand (COD). The errors of measured data were −137 m3/day (−4.41 %) and 281 kg/day (7.92 %) for flow and COD, respectively. According to the balanced data, the removal rates of COD and 5-day biological oxygen demand (BOD5) through the aeration unit were equal to 37 and 46 %, respectively. In addition, the COD and BOD5 concentrations were reduced by about 61.9 % (2137 kg/day) and 78.1 % (1976 kg/day), respectively, prior to the biological process. At the same time, the removal rates of benzene, toluene, and styrene were 56, 38, and 69%,respectively.Theresultsrevealedthatabout40%ofinfluent benzene(75.5kg/day)isemittedtotheambientairattheoverhead oftheequalizationbasin.Itcanbeconcludedthatthevolatilization of organic compounds is the basic mechanism for the removal of volatile organic compounds (VOCs) and it corresponds to the main part of total COD removal from the WWTP.

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نویسنده نفر چندم مقاله
محمد شاکرخطیبیدوم
رضا دهقانزاده ریحانیسوم

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behnami paper ESPR.pdf1395/06/23571977دانلود