Submerged upflow biotower operation and computer simulation
A two step operation is proposed for the biodegradation of low concentrations (< 10 mg/L) of BETX substances in an up flow submerged biotower configuration. Step 1 involves growth of a lush biofilm using benzoic acid in a batch mode. Step 2 involves a longer term biological transformation of BETX...
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Veröffentlicht in: | Water science and technology 1994-01, Vol.30 (11), p.143-146 |
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creator | Neufeld, R D Badali, CA Powers, D Carson, C |
description | A two step operation is proposed for the biodegradation of low concentrations (< 10 mg/L) of BETX substances in an up flow submerged biotower configuration. Step 1 involves growth of a lush biofilm using benzoic acid in a batch mode. Step 2 involves a longer term biological transformation of BETX. Kinetics of biotransformations are modeled using first order assumptions, with rate constants being a function of benzoic acid dosages used in Step 1. A calibrated computer model is developed and presented to predict the degree of transformation and biomass level throughout the tower under a variety of inlet and design operational conditions. |
doi_str_mv | 10.2166/wst.1994.0554 |
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Step 1 involves growth of a lush biofilm using benzoic acid in a batch mode. Step 2 involves a longer term biological transformation of BETX. Kinetics of biotransformations are modeled using first order assumptions, with rate constants being a function of benzoic acid dosages used in Step 1. A calibrated computer model is developed and presented to predict the degree of transformation and biomass level throughout the tower under a variety of inlet and design operational conditions.</description><subject>Benzoic acid</subject><subject>Biodegradation</subject><subject>Biofilms</subject><subject>Biotransformation</subject><subject>Computer simulation</subject><subject>Constants</subject><subject>Inlets (waterways)</subject><subject>Kinetics</subject><subject>Low concentrations</subject><subject>Rate constants</subject><issn>0273-1223</issn><issn>1996-9732</issn><isbn>0080426322</isbn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1994</creationdate><recordtype>article</recordtype><sourceid>BENPR</sourceid><recordid>eNqNkUtLxDAURoMPcGZ06b4guOuYdxpcyeALBlyo65DmIR3apiYtg__ejOPKzbi6l4_D5eMeAC4RXGLE-c02jUskJV1CxugRmOWdl1IQfAzmEFaQYk4wPgEziAUpEcbkDMxT2kAIBaFwBm5fp7pz8cPZYhp8G7ZF3YQxbF0swuCiHpvQF7q3hQndMI05Tk03tT_5OTj1uk3u4ncuwPvD_dvqqVy_PD6v7talIZSMpa2p9N5CaHzlnZDWGeuFtqQyRFfcYI2dqRFDuW9uazHSXBAtmJbEYobIAlzv7w4xfE4ujaprknFtq3sXpqSwrATjHP8D5FhKyA6CiFc0v0ceBglnuWyVwas_4CZMsc9vUUhSQqCUgmeq3FMmhpSi82qITafjl0JQ7YSqLFTthKqdUPINMx-ROQ</recordid><startdate>19940101</startdate><enddate>19940101</enddate><creator>Neufeld, R D</creator><creator>Badali, CA</creator><creator>Powers, D</creator><creator>Carson, C</creator><general>IWA Publishing</general><scope>AAYXX</scope><scope>CITATION</scope><scope>3V.</scope><scope>7QH</scope><scope>7UA</scope><scope>7X7</scope><scope>7XB</scope><scope>88E</scope><scope>8FE</scope><scope>8FG</scope><scope>8FI</scope><scope>8FJ</scope><scope>8FK</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AEUYN</scope><scope>AFKRA</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>BHPHI</scope><scope>BKSAR</scope><scope>C1K</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>F1W</scope><scope>FYUFA</scope><scope>GHDGH</scope><scope>H96</scope><scope>H97</scope><scope>HCIFZ</scope><scope>K9.</scope><scope>L.G</scope><scope>L6V</scope><scope>M0S</scope><scope>M1P</scope><scope>M7S</scope><scope>PCBAR</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PTHSS</scope><scope>7QO</scope><scope>7T7</scope><scope>7TV</scope><scope>8FD</scope><scope>FR3</scope><scope>P64</scope><scope>7TB</scope><scope>KR7</scope></search><sort><creationdate>19940101</creationdate><title>Submerged upflow biotower operation and computer simulation</title><author>Neufeld, R D ; 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Step 1 involves growth of a lush biofilm using benzoic acid in a batch mode. Step 2 involves a longer term biological transformation of BETX. Kinetics of biotransformations are modeled using first order assumptions, with rate constants being a function of benzoic acid dosages used in Step 1. A calibrated computer model is developed and presented to predict the degree of transformation and biomass level throughout the tower under a variety of inlet and design operational conditions.</abstract><cop>London</cop><pub>IWA Publishing</pub><doi>10.2166/wst.1994.0554</doi><tpages>4</tpages></addata></record> |
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language | eng |
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source | EZB-FREE-00999 freely available EZB journals |
subjects | Benzoic acid Biodegradation Biofilms Biotransformation Computer simulation Constants Inlets (waterways) Kinetics Low concentrations Rate constants |
title | Submerged upflow biotower operation and computer simulation |
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