A kinetic study on anaerobic reduction of sulphate, Part I: Effect of sulphate concentration
The kinetics of anaerobic reduction of sulphate was studied in continuous bioreactors. The effects of initial sulphate concentration and its volumetric loading on the kinetics of reaction and activity of sulphate-reducing bacteria were investigated. The increase in initial concentration of sulphate...
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description | The kinetics of anaerobic reduction of sulphate was studied in continuous bioreactors. The effects of initial sulphate concentration and its volumetric loading on the kinetics of reaction and activity of sulphate-reducing bacteria were investigated. The increase in initial concentration of sulphate in the range 1.0–
10.0
kg
m
−3
enhanced the reaction rate from 0.007–
0.17
kg
m
−3
h
−1
. For a given initial sulphate concentration increasing the volumetric loading rate of sulphate led to a linear increase in volumetric reduction rate. The initial concentration of sulphate did not have a significant effect on maximum specific growth rate (
μ
m
), decay coefficient (
k
d
) on bacterial yields (
Y
x/sulphate
and
Y
x/acetate
), with the values of these coefficients being
0.061,
0.035
h
−1,
0.567
g
bacteria/g sulphate and
0.572
g
bacteria/g acetate, respectively. The saturation constant (
K
s
) was an increasing linear function of initial sulphate concentration, with the lowest and highest values being 0.027 and
0.125
kg
m
−3
, respectively. Using the experimental data a kinetic model, incorporating terms for the effects of initial and residual concentrations of sulphate and biomass, was developed. |
doi_str_mv | 10.1016/S0009-2509(02)00152-5 |
format | Article |
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10.0
kg
m
−3
enhanced the reaction rate from 0.007–
0.17
kg
m
−3
h
−1
. For a given initial sulphate concentration increasing the volumetric loading rate of sulphate led to a linear increase in volumetric reduction rate. The initial concentration of sulphate did not have a significant effect on maximum specific growth rate (
μ
m
), decay coefficient (
k
d
) on bacterial yields (
Y
x/sulphate
and
Y
x/acetate
), with the values of these coefficients being
0.061,
0.035
h
−1,
0.567
g
bacteria/g sulphate and
0.572
g
bacteria/g acetate, respectively. The saturation constant (
K
s
) was an increasing linear function of initial sulphate concentration, with the lowest and highest values being 0.027 and
0.125
kg
m
−3
, respectively. Using the experimental data a kinetic model, incorporating terms for the effects of initial and residual concentrations of sulphate and biomass, was developed.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/S0009-2509(02)00152-5</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Anaerobic digestion ; Applied sciences ; Bacteria ; Biological and medical sciences ; Biological treatment of waters ; Biomass ; Bioremediation ; Biotechnology ; Continuous bioreactor ; Environment and pollution ; Exact sciences and technology ; Fundamental and applied biological sciences. Psychology ; Industrial applications and implications. Economical aspects ; Industrial wastewaters ; Kinetics ; Mathematical modeling ; Pollution ; Reaction kinetics ; Reduction ; Sulphate concentration ; Sulphate-reducing bacteria ; Wastewaters ; Water treatment and pollution</subject><ispartof>Chemical engineering science, 2002-07, Vol.57 (14), p.2773-2780</ispartof><rights>2002 Elsevier Science Ltd</rights><rights>2002 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c399t-49571222b9cc32416364ba604bc894c0eae84b52d944e369666f3c97228b8b3c3</citedby><cites>FETCH-LOGICAL-c399t-49571222b9cc32416364ba604bc894c0eae84b52d944e369666f3c97228b8b3c3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/S0009-2509(02)00152-5$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>315,781,785,3551,27929,27930,46000</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=13794511$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Moosa, S.</creatorcontrib><creatorcontrib>Nemati, M.</creatorcontrib><creatorcontrib>T. L. Harrison, S.</creatorcontrib><title>A kinetic study on anaerobic reduction of sulphate, Part I: Effect of sulphate concentration</title><title>Chemical engineering science</title><description>The kinetics of anaerobic reduction of sulphate was studied in continuous bioreactors. The effects of initial sulphate concentration and its volumetric loading on the kinetics of reaction and activity of sulphate-reducing bacteria were investigated. The increase in initial concentration of sulphate in the range 1.0–
10.0
kg
m
−3
enhanced the reaction rate from 0.007–
0.17
kg
m
−3
h
−1
. For a given initial sulphate concentration increasing the volumetric loading rate of sulphate led to a linear increase in volumetric reduction rate. The initial concentration of sulphate did not have a significant effect on maximum specific growth rate (
μ
m
), decay coefficient (
k
d
) on bacterial yields (
Y
x/sulphate
and
Y
x/acetate
), with the values of these coefficients being
0.061,
0.035
h
−1,
0.567
g
bacteria/g sulphate and
0.572
g
bacteria/g acetate, respectively. The saturation constant (
K
s
) was an increasing linear function of initial sulphate concentration, with the lowest and highest values being 0.027 and
0.125
kg
m
−3
, respectively. Using the experimental data a kinetic model, incorporating terms for the effects of initial and residual concentrations of sulphate and biomass, was developed.</description><subject>Anaerobic digestion</subject><subject>Applied sciences</subject><subject>Bacteria</subject><subject>Biological and medical sciences</subject><subject>Biological treatment of waters</subject><subject>Biomass</subject><subject>Bioremediation</subject><subject>Biotechnology</subject><subject>Continuous bioreactor</subject><subject>Environment and pollution</subject><subject>Exact sciences and technology</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Industrial applications and implications. Economical aspects</subject><subject>Industrial wastewaters</subject><subject>Kinetics</subject><subject>Mathematical modeling</subject><subject>Pollution</subject><subject>Reaction kinetics</subject><subject>Reduction</subject><subject>Sulphate concentration</subject><subject>Sulphate-reducing bacteria</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2002</creationdate><recordtype>article</recordtype><recordid>eNqFkE1LHEEQhpugkFXzEwJ9iRhwTH_PtBcRWT9gwUCSW6DpqakhnYwza3dPwH9vryvqzVNRVc9bBQ8hnzk74Yybbz8YY7YSmtkjJr4yxrWo9Aey4E0tK6WY3iGLF-Qj2Uvpb2nrmrMF-X1O_4URcwCa8tw90GmkfvQYp7aMInYz5FBmU0_TPKz_-IzH9LuPmd6c0mXfI-S3OwrTCDjm6DepA7Lb-yHhp-e6T35dLn9eXFer26ubi_NVBdLaXCmray6EaC2AFIobaVTrDVMtNFYBQ4-NarXorFIojTXG9BJsLUTTNq0EuU8Ot3fXcbqfMWV3FxLgMPgRpzk5UfPaCi7eB7kqZ40qoN6CEKeUIvZuHcOdjw-OM7eR7p6ku41Rx4R7ku50yX15fuAT-KGPfoSQXsOytkpzXrizLYdFy_-A0SUIWNR1IRalrpvCO58eATrulKU</recordid><startdate>20020701</startdate><enddate>20020701</enddate><creator>Moosa, S.</creator><creator>Nemati, M.</creator><creator>T. L. Harrison, S.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope></search><sort><creationdate>20020701</creationdate><title>A kinetic study on anaerobic reduction of sulphate, Part I: Effect of sulphate concentration</title><author>Moosa, S. ; Nemati, M. ; T. L. Harrison, S.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c399t-49571222b9cc32416364ba604bc894c0eae84b52d944e369666f3c97228b8b3c3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2002</creationdate><topic>Anaerobic digestion</topic><topic>Applied sciences</topic><topic>Bacteria</topic><topic>Biological and medical sciences</topic><topic>Biological treatment of waters</topic><topic>Biomass</topic><topic>Bioremediation</topic><topic>Biotechnology</topic><topic>Continuous bioreactor</topic><topic>Environment and pollution</topic><topic>Exact sciences and technology</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Industrial applications and implications. Economical aspects</topic><topic>Industrial wastewaters</topic><topic>Kinetics</topic><topic>Mathematical modeling</topic><topic>Pollution</topic><topic>Reaction kinetics</topic><topic>Reduction</topic><topic>Sulphate concentration</topic><topic>Sulphate-reducing bacteria</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Moosa, S.</creatorcontrib><creatorcontrib>Nemati, M.</creatorcontrib><creatorcontrib>T. L. Harrison, S.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Moosa, S.</au><au>Nemati, M.</au><au>T. L. Harrison, S.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A kinetic study on anaerobic reduction of sulphate, Part I: Effect of sulphate concentration</atitle><jtitle>Chemical engineering science</jtitle><date>2002-07-01</date><risdate>2002</risdate><volume>57</volume><issue>14</issue><spage>2773</spage><epage>2780</epage><pages>2773-2780</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>The kinetics of anaerobic reduction of sulphate was studied in continuous bioreactors. The effects of initial sulphate concentration and its volumetric loading on the kinetics of reaction and activity of sulphate-reducing bacteria were investigated. The increase in initial concentration of sulphate in the range 1.0–
10.0
kg
m
−3
enhanced the reaction rate from 0.007–
0.17
kg
m
−3
h
−1
. For a given initial sulphate concentration increasing the volumetric loading rate of sulphate led to a linear increase in volumetric reduction rate. The initial concentration of sulphate did not have a significant effect on maximum specific growth rate (
μ
m
), decay coefficient (
k
d
) on bacterial yields (
Y
x/sulphate
and
Y
x/acetate
), with the values of these coefficients being
0.061,
0.035
h
−1,
0.567
g
bacteria/g sulphate and
0.572
g
bacteria/g acetate, respectively. The saturation constant (
K
s
) was an increasing linear function of initial sulphate concentration, with the lowest and highest values being 0.027 and
0.125
kg
m
−3
, respectively. Using the experimental data a kinetic model, incorporating terms for the effects of initial and residual concentrations of sulphate and biomass, was developed.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/S0009-2509(02)00152-5</doi><tpages>8</tpages></addata></record> |
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source | Access via ScienceDirect (Elsevier) |
subjects | Anaerobic digestion Applied sciences Bacteria Biological and medical sciences Biological treatment of waters Biomass Bioremediation Biotechnology Continuous bioreactor Environment and pollution Exact sciences and technology Fundamental and applied biological sciences. Psychology Industrial applications and implications. Economical aspects Industrial wastewaters Kinetics Mathematical modeling Pollution Reaction kinetics Reduction Sulphate concentration Sulphate-reducing bacteria Wastewaters Water treatment and pollution |
title | A kinetic study on anaerobic reduction of sulphate, Part I: Effect of sulphate concentration |
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