Comparison of two continuous fungal bioreactors for posttreatment of anaerobically pretreated weak black liquor from kraft pulp mills
The purpose of this work was to evaluate and compare two continuous systems of posttreatment of anaerobically pretreated weak black liquor (WBL). The first system consisted of a packed bed reactor (PBR) with Trametes versicolor (Tv) immobilized on wood cubes of holm oak (biocubes). The second system...
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creator | Ortega-Clemente, Alfredo Marín-Mezo, G. Ponce-Noyola, M.T. Montes-Horcasitas, M.C. Caffarel-Méndez, S. Barrera-Cortés, Josefina Poggi-Varaldo, Héctor M. |
description | The purpose of this work was to evaluate and compare two continuous systems of posttreatment of anaerobically pretreated weak black liquor (WBL). The first system consisted of a packed bed reactor (PBR) with Trametes versicolor (Tv) immobilized on wood cubes of holm oak (biocubes). The second system was a fluidized bed reactor (FBR) with Lentinus edodes (Le) immobilized on wood cubes of holm oak. The reactors operated for 65 days at a hydraulic retention time (HRT) of 5 days, at 28°C, with continuous aeration. Response variables monitored were conventional and specific, unit, net removal efficiency (η and ηsun, respectively) of chemical oxygen demand (COD), color, and ligninoids, and enzymatic activities of manganese peroxidase (MnP), lignin peroxidase (LiP), laccase (Lac) and proteases. The PBR showed an average color η superior to that of the FBR (52.42 ± 21.78% and 25.34 ± 14.38% for PBR and FBR, respectively); removals of COD and ligninoids presented a similar pattern to that of color. Lac activity was significantly larger in PBR than in FBR. Activity of MnP in PBR was higher than that of the FBR (0.004 and 0.002 U MnP/mL, respectively). This difference could be ascribed to the different fungi present in each bioreactor. LiP activity was very low in both reactors. Average value of proteases was almost double in the FBR as compared with PBR (0.472 and 0.209 U Proteases/mL, respectively). During the last 2 weeks of operation, biocubes in the FBR experienced a significant loss of the attached Le biomass, probably by attrition. This and higher protease activity in the FBR could explain the lower pollutant removals achieved in the FBR. Overall, PBR with immobilized Tv showed a better performance than the FBR with Le for the posttreatment of the recalcitrant anaerobic effluent. Extended and sustained pollutant removal (65 days) was achieved in the PBR, although more research is needed to evaluate bioreactor performance at shorter hydraulic retention times. Biotechnol. Bioeng. 2007;96:640–650. © 2006 Wiley Periodicals, Inc. |
doi_str_mv | 10.1002/bit.21134 |
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The first system consisted of a packed bed reactor (PBR) with Trametes versicolor (Tv) immobilized on wood cubes of holm oak (biocubes). The second system was a fluidized bed reactor (FBR) with Lentinus edodes (Le) immobilized on wood cubes of holm oak. The reactors operated for 65 days at a hydraulic retention time (HRT) of 5 days, at 28°C, with continuous aeration. Response variables monitored were conventional and specific, unit, net removal efficiency (η and ηsun, respectively) of chemical oxygen demand (COD), color, and ligninoids, and enzymatic activities of manganese peroxidase (MnP), lignin peroxidase (LiP), laccase (Lac) and proteases. The PBR showed an average color η superior to that of the FBR (52.42 ± 21.78% and 25.34 ± 14.38% for PBR and FBR, respectively); removals of COD and ligninoids presented a similar pattern to that of color. Lac activity was significantly larger in PBR than in FBR. Activity of MnP in PBR was higher than that of the FBR (0.004 and 0.002 U MnP/mL, respectively). This difference could be ascribed to the different fungi present in each bioreactor. LiP activity was very low in both reactors. Average value of proteases was almost double in the FBR as compared with PBR (0.472 and 0.209 U Proteases/mL, respectively). During the last 2 weeks of operation, biocubes in the FBR experienced a significant loss of the attached Le biomass, probably by attrition. This and higher protease activity in the FBR could explain the lower pollutant removals achieved in the FBR. Overall, PBR with immobilized Tv showed a better performance than the FBR with Le for the posttreatment of the recalcitrant anaerobic effluent. Extended and sustained pollutant removal (65 days) was achieved in the PBR, although more research is needed to evaluate bioreactor performance at shorter hydraulic retention times. Biotechnol. Bioeng. 2007;96:640–650. © 2006 Wiley Periodicals, Inc.</description><identifier>ISSN: 0006-3592</identifier><identifier>EISSN: 1097-0290</identifier><identifier>DOI: 10.1002/bit.21134</identifier><identifier>PMID: 16937406</identifier><identifier>CODEN: BIBIAU</identifier><language>eng</language><publisher>Hoboken: Wiley Subscription Services, Inc., A Wiley Company</publisher><subject>aerobic ; Agaricales - metabolism ; Basidiomycota - metabolism ; biocubes ; Biodegradation, Environmental ; Biological and medical sciences ; Bioreactors ; Biotechnology ; fluidized bed reactor ; Fluidized bed reactors ; Fundamental and applied biological sciences. Psychology ; Fungi ; Industrial Waste ; Kraft wastewater ; Lignin - metabolism ; ligninolytic fungus ; Liquor ; packed bed reactor ; Packed bed reactors ; posttreatment ; Trametes versicolor ; Waste Disposal, Fluid - methods ; Water Purification - methods ; Wood ; Wood - microbiology</subject><ispartof>Biotechnology and bioengineering, 2007-03, Vol.96 (4), p.640-650</ispartof><rights>Copyright © 2006 Wiley Periodicals, Inc.</rights><rights>2007 INIST-CNRS</rights><rights>Copyright John Wiley and Sons, Limited Mar 1, 2007</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c5214-ee8e9caf958d06f14902e4830deaf02a9bbf47750375848482f51315eb0ed4283</citedby><cites>FETCH-LOGICAL-c5214-ee8e9caf958d06f14902e4830deaf02a9bbf47750375848482f51315eb0ed4283</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://onlinelibrary.wiley.com/doi/pdf/10.1002%2Fbit.21134$$EPDF$$P50$$Gwiley$$H</linktopdf><linktohtml>$$Uhttps://onlinelibrary.wiley.com/doi/full/10.1002%2Fbit.21134$$EHTML$$P50$$Gwiley$$H</linktohtml><link.rule.ids>314,776,780,1411,27901,27902,45550,45551</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=18548076$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/16937406$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Ortega-Clemente, Alfredo</creatorcontrib><creatorcontrib>Marín-Mezo, G.</creatorcontrib><creatorcontrib>Ponce-Noyola, M.T.</creatorcontrib><creatorcontrib>Montes-Horcasitas, M.C.</creatorcontrib><creatorcontrib>Caffarel-Méndez, S.</creatorcontrib><creatorcontrib>Barrera-Cortés, Josefina</creatorcontrib><creatorcontrib>Poggi-Varaldo, Héctor M.</creatorcontrib><title>Comparison of two continuous fungal bioreactors for posttreatment of anaerobically pretreated weak black liquor from kraft pulp mills</title><title>Biotechnology and bioengineering</title><addtitle>Biotechnol. Bioeng</addtitle><description>The purpose of this work was to evaluate and compare two continuous systems of posttreatment of anaerobically pretreated weak black liquor (WBL). The first system consisted of a packed bed reactor (PBR) with Trametes versicolor (Tv) immobilized on wood cubes of holm oak (biocubes). The second system was a fluidized bed reactor (FBR) with Lentinus edodes (Le) immobilized on wood cubes of holm oak. The reactors operated for 65 days at a hydraulic retention time (HRT) of 5 days, at 28°C, with continuous aeration. Response variables monitored were conventional and specific, unit, net removal efficiency (η and ηsun, respectively) of chemical oxygen demand (COD), color, and ligninoids, and enzymatic activities of manganese peroxidase (MnP), lignin peroxidase (LiP), laccase (Lac) and proteases. The PBR showed an average color η superior to that of the FBR (52.42 ± 21.78% and 25.34 ± 14.38% for PBR and FBR, respectively); removals of COD and ligninoids presented a similar pattern to that of color. Lac activity was significantly larger in PBR than in FBR. Activity of MnP in PBR was higher than that of the FBR (0.004 and 0.002 U MnP/mL, respectively). This difference could be ascribed to the different fungi present in each bioreactor. LiP activity was very low in both reactors. Average value of proteases was almost double in the FBR as compared with PBR (0.472 and 0.209 U Proteases/mL, respectively). During the last 2 weeks of operation, biocubes in the FBR experienced a significant loss of the attached Le biomass, probably by attrition. This and higher protease activity in the FBR could explain the lower pollutant removals achieved in the FBR. Overall, PBR with immobilized Tv showed a better performance than the FBR with Le for the posttreatment of the recalcitrant anaerobic effluent. Extended and sustained pollutant removal (65 days) was achieved in the PBR, although more research is needed to evaluate bioreactor performance at shorter hydraulic retention times. Biotechnol. Bioeng. 2007;96:640–650. © 2006 Wiley Periodicals, Inc.</description><subject>aerobic</subject><subject>Agaricales - metabolism</subject><subject>Basidiomycota - metabolism</subject><subject>biocubes</subject><subject>Biodegradation, Environmental</subject><subject>Biological and medical sciences</subject><subject>Bioreactors</subject><subject>Biotechnology</subject><subject>fluidized bed reactor</subject><subject>Fluidized bed reactors</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Fungi</subject><subject>Industrial Waste</subject><subject>Kraft wastewater</subject><subject>Lignin - metabolism</subject><subject>ligninolytic fungus</subject><subject>Liquor</subject><subject>packed bed reactor</subject><subject>Packed bed reactors</subject><subject>posttreatment</subject><subject>Trametes versicolor</subject><subject>Waste Disposal, Fluid - methods</subject><subject>Water Purification - methods</subject><subject>Wood</subject><subject>Wood - microbiology</subject><issn>0006-3592</issn><issn>1097-0290</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2007</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqFkd-K1DAUxoso7rh64QtIEBS86G7-tWkunVHHhUFvVvYypO2JZCdtuknKOA_ge5vZGV0QRHIRcvL7vsM5X1G8JPiCYEwvW5suKCGMPyoWBEtRYirx42KBMa5LVkl6VjyL8TY_RVPXT4szUksmOK4Xxc-VHyYdbPQj8galnUedH5MdZz9HZObxu3aotT6A7pIPueQDmnxMKVfSAGM6yPSoIfjWdtq5PZoC3P9Cj3agt6h1utsiZ-_mrDXBD2gbtElomt2EButcfF48MdpFeHG6z4tvnz5erz6Xm6_rq9X7TdlVlPASoAHZaSOrpse1IVxiCrxhuAdtMNWybQ0XosJMVA3Ph5qKMFJBi6HntGHnxduj7xT83QwxqcHGDpzTI-R5Fcsr4pVk_wWJbGqRN5vB13-Bt34OYx5CUcJETQU_uL07Ql3wMQYwagp20GGvCFaHBFVOUN0nmNlXJ8O5HaB_IE-RZeDNCdAx79sEPXY2PnBNxRssDtzlkdtZB_t_d1TLq-vfrcujwsYEP_4odNiqPKyo1M2XtVquP9wspdgown4BnNLCwg</recordid><startdate>20070301</startdate><enddate>20070301</enddate><creator>Ortega-Clemente, Alfredo</creator><creator>Marín-Mezo, G.</creator><creator>Ponce-Noyola, M.T.</creator><creator>Montes-Horcasitas, M.C.</creator><creator>Caffarel-Méndez, S.</creator><creator>Barrera-Cortés, Josefina</creator><creator>Poggi-Varaldo, Héctor M.</creator><general>Wiley Subscription Services, Inc., A Wiley Company</general><general>Wiley</general><general>Wiley Subscription Services, Inc</general><scope>BSCLL</scope><scope>IQODW</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope><scope>M7N</scope></search><sort><creationdate>20070301</creationdate><title>Comparison of two continuous fungal bioreactors for posttreatment of anaerobically pretreated weak black liquor from kraft pulp mills</title><author>Ortega-Clemente, Alfredo ; Marín-Mezo, G. ; Ponce-Noyola, M.T. ; Montes-Horcasitas, M.C. ; Caffarel-Méndez, S. ; Barrera-Cortés, Josefina ; Poggi-Varaldo, Héctor M.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c5214-ee8e9caf958d06f14902e4830deaf02a9bbf47750375848482f51315eb0ed4283</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2007</creationdate><topic>aerobic</topic><topic>Agaricales - metabolism</topic><topic>Basidiomycota - metabolism</topic><topic>biocubes</topic><topic>Biodegradation, Environmental</topic><topic>Biological and medical sciences</topic><topic>Bioreactors</topic><topic>Biotechnology</topic><topic>fluidized bed reactor</topic><topic>Fluidized bed reactors</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Fungi</topic><topic>Industrial Waste</topic><topic>Kraft wastewater</topic><topic>Lignin - metabolism</topic><topic>ligninolytic fungus</topic><topic>Liquor</topic><topic>packed bed reactor</topic><topic>Packed bed reactors</topic><topic>posttreatment</topic><topic>Trametes versicolor</topic><topic>Waste Disposal, Fluid - methods</topic><topic>Water Purification - methods</topic><topic>Wood</topic><topic>Wood - microbiology</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ortega-Clemente, Alfredo</creatorcontrib><creatorcontrib>Marín-Mezo, G.</creatorcontrib><creatorcontrib>Ponce-Noyola, M.T.</creatorcontrib><creatorcontrib>Montes-Horcasitas, M.C.</creatorcontrib><creatorcontrib>Caffarel-Méndez, S.</creatorcontrib><creatorcontrib>Barrera-Cortés, Josefina</creatorcontrib><creatorcontrib>Poggi-Varaldo, Héctor M.</creatorcontrib><collection>Istex</collection><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>Biotechnology Research Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Computer and Information Systems Abstracts</collection><collection>Corrosion Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Materials Business File</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Copper Technical Reference Library</collection><collection>Materials Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>Algology Mycology and Protozoology Abstracts (Microbiology C)</collection><jtitle>Biotechnology and bioengineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ortega-Clemente, Alfredo</au><au>Marín-Mezo, G.</au><au>Ponce-Noyola, M.T.</au><au>Montes-Horcasitas, M.C.</au><au>Caffarel-Méndez, S.</au><au>Barrera-Cortés, Josefina</au><au>Poggi-Varaldo, Héctor M.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Comparison of two continuous fungal bioreactors for posttreatment of anaerobically pretreated weak black liquor from kraft pulp mills</atitle><jtitle>Biotechnology and bioengineering</jtitle><addtitle>Biotechnol. Bioeng</addtitle><date>2007-03-01</date><risdate>2007</risdate><volume>96</volume><issue>4</issue><spage>640</spage><epage>650</epage><pages>640-650</pages><issn>0006-3592</issn><eissn>1097-0290</eissn><coden>BIBIAU</coden><abstract>The purpose of this work was to evaluate and compare two continuous systems of posttreatment of anaerobically pretreated weak black liquor (WBL). The first system consisted of a packed bed reactor (PBR) with Trametes versicolor (Tv) immobilized on wood cubes of holm oak (biocubes). The second system was a fluidized bed reactor (FBR) with Lentinus edodes (Le) immobilized on wood cubes of holm oak. The reactors operated for 65 days at a hydraulic retention time (HRT) of 5 days, at 28°C, with continuous aeration. Response variables monitored were conventional and specific, unit, net removal efficiency (η and ηsun, respectively) of chemical oxygen demand (COD), color, and ligninoids, and enzymatic activities of manganese peroxidase (MnP), lignin peroxidase (LiP), laccase (Lac) and proteases. The PBR showed an average color η superior to that of the FBR (52.42 ± 21.78% and 25.34 ± 14.38% for PBR and FBR, respectively); removals of COD and ligninoids presented a similar pattern to that of color. Lac activity was significantly larger in PBR than in FBR. Activity of MnP in PBR was higher than that of the FBR (0.004 and 0.002 U MnP/mL, respectively). This difference could be ascribed to the different fungi present in each bioreactor. LiP activity was very low in both reactors. Average value of proteases was almost double in the FBR as compared with PBR (0.472 and 0.209 U Proteases/mL, respectively). During the last 2 weeks of operation, biocubes in the FBR experienced a significant loss of the attached Le biomass, probably by attrition. This and higher protease activity in the FBR could explain the lower pollutant removals achieved in the FBR. Overall, PBR with immobilized Tv showed a better performance than the FBR with Le for the posttreatment of the recalcitrant anaerobic effluent. Extended and sustained pollutant removal (65 days) was achieved in the PBR, although more research is needed to evaluate bioreactor performance at shorter hydraulic retention times. Biotechnol. Bioeng. 2007;96:640–650. © 2006 Wiley Periodicals, Inc.</abstract><cop>Hoboken</cop><pub>Wiley Subscription Services, Inc., A Wiley Company</pub><pmid>16937406</pmid><doi>10.1002/bit.21134</doi><tpages>11</tpages></addata></record> |
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subjects | aerobic Agaricales - metabolism Basidiomycota - metabolism biocubes Biodegradation, Environmental Biological and medical sciences Bioreactors Biotechnology fluidized bed reactor Fluidized bed reactors Fundamental and applied biological sciences. Psychology Fungi Industrial Waste Kraft wastewater Lignin - metabolism ligninolytic fungus Liquor packed bed reactor Packed bed reactors posttreatment Trametes versicolor Waste Disposal, Fluid - methods Water Purification - methods Wood Wood - microbiology |
title | Comparison of two continuous fungal bioreactors for posttreatment of anaerobically pretreated weak black liquor from kraft pulp mills |
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