Anaerobic treatment of olive mill wastewater with digested piggery effluent
Anaerobic digestion of olive mill wastewater (OMW) in admixture with anaerobically digested piggery effluent (ADPE) was investigated. Successive volumetric increases of OMW ranging from 8 to 91% were mixed with ADPE and treated through an upflow anaerobic filter to promote gradual adaptation of the...
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description | Anaerobic digestion of olive mill wastewater (OMW) in admixture with anaerobically digested piggery effluent (ADPE) was investigated. Successive volumetric increases of OMW ranging from 8 to 91% were mixed with ADPE and treated through an upflow anaerobic filter to promote gradual adaptation of the microbial consortium. The response of the digester was positive, and only at 91% v/v OMW was lower reactor performance obtained, suggesting that a concentration on the order of 83% v/v was the highest in terms of the efficiency and stability of the reactor. At this inlet composition, the mixture loading rate varied from 5.0 to 5.7 kg chemical oxygen demand$({\rm COD})/{\rm m}^{3}\cdot {\rm d}$and the total COD removal was 73 to 75%, with a gas production of 1.7 to 2.1${\rm m}^{3}/{\rm m}^{3}\cdot {\rm d}$(66 to 68%${\rm CH}_{4}$). The corresponding volume of ADPE (17%) was enough to maintain an influent ammonium-nitrogen$({\rm NH}_{4}{}^{+}\text{-}{\rm N})$concentration of 0.17 to 0.19 kg${\rm NH}_{4}{}^{+}\text{-}{\rm N}/{\rm m}^{3}$, which was practically spent. |
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Successive volumetric increases of OMW ranging from 8 to 91% were mixed with ADPE and treated through an upflow anaerobic filter to promote gradual adaptation of the microbial consortium. The response of the digester was positive, and only at 91% v/v OMW was lower reactor performance obtained, suggesting that a concentration on the order of 83% v/v was the highest in terms of the efficiency and stability of the reactor. At this inlet composition, the mixture loading rate varied from 5.0 to 5.7 kg chemical oxygen demand$({\rm COD})/{\rm m}^{3}\cdot {\rm d}$and the total COD removal was 73 to 75%, with a gas production of 1.7 to 2.1${\rm m}^{3}/{\rm m}^{3}\cdot {\rm d}$(66 to 68%${\rm CH}_{4}$). The corresponding volume of ADPE (17%) was enough to maintain an influent ammonium-nitrogen$({\rm NH}_{4}{}^{+}\text{-}{\rm N})$concentration of 0.17 to 0.19 kg${\rm NH}_{4}{}^{+}\text{-}{\rm N}/{\rm m}^{3}$, which was practically spent.</description><identifier>ISSN: 1061-4303</identifier><identifier>EISSN: 1554-7531</identifier><identifier>DOI: 10.2175/106143098X123390</identifier><language>eng</language><publisher>Alexandria, VA: Water Environment Federation</publisher><subject>ANAEROBIC DIGESTION ; ANAEROBIC FILTER ; ANAEROBIC TREATMENT ; Applied sciences ; Biological and medical sciences ; Biological treatment of waters ; Biotechnology ; Chemical oxygen demand ; Environment and pollution ; Exact sciences and technology ; FACTORIES ; FATS ; Fundamental and applied biological sciences. Psychology ; GAS PRODUCTION ; Industrial applications and implications. Economical aspects ; Industrial effluents ; Industrial wastewaters ; Loading rate ; LOADING RATIO ; MEASUREMENT ; Methane ; METHANE FERMENTATION ; MIXTURES ; OILS INDUSTRY ; OLIVE MILL WASTEWATER ; OLIVE OIL ; Pig housing ; PIGGERIES ; PIGGERY EFFLUENT ; POLLUTANT LOAD ; Pollution ; REMOVAL ; Research Papers ; VOLATILE FATTY ACIDS ; WASTEWATER ; WASTEWATER TREATMENT ; Wastewaters ; Water treatment and pollution</subject><ispartof>Water environment research, 1998-07, Vol.70 (5), p.1056-1061</ispartof><rights>Copyright 1998 The Water Environment Federation (WEF)</rights><rights>1998 Water Environment Federation</rights><rights>1998 INIST-CNRS</rights><rights>Copyright Water Environment Federation Jul/Aug 1998</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c4246-4a886105ecf390c622b8e9912d5c34aa1a3fb6d5d232667f9b27fd271454df963</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.jstor.org/stable/pdf/25045117$$EPDF$$P50$$Gjstor$$H</linktopdf><linktohtml>$$Uhttps://www.jstor.org/stable/25045117$$EHTML$$P50$$Gjstor$$H</linktohtml><link.rule.ids>314,780,784,803,1417,27924,27925,45574,45575,58017,58250</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=2353859$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Marques, I.P</creatorcontrib><creatorcontrib>Teixeira, A</creatorcontrib><creatorcontrib>Rodrigues, L</creatorcontrib><creatorcontrib>Martins Dias, S</creatorcontrib><creatorcontrib>Novais, J.M</creatorcontrib><title>Anaerobic treatment of olive mill wastewater with digested piggery effluent</title><title>Water environment research</title><description>Anaerobic digestion of olive mill wastewater (OMW) in admixture with anaerobically digested piggery effluent (ADPE) was investigated. Successive volumetric increases of OMW ranging from 8 to 91% were mixed with ADPE and treated through an upflow anaerobic filter to promote gradual adaptation of the microbial consortium. The response of the digester was positive, and only at 91% v/v OMW was lower reactor performance obtained, suggesting that a concentration on the order of 83% v/v was the highest in terms of the efficiency and stability of the reactor. At this inlet composition, the mixture loading rate varied from 5.0 to 5.7 kg chemical oxygen demand$({\rm COD})/{\rm m}^{3}\cdot {\rm d}$and the total COD removal was 73 to 75%, with a gas production of 1.7 to 2.1${\rm m}^{3}/{\rm m}^{3}\cdot {\rm d}$(66 to 68%${\rm CH}_{4}$). The corresponding volume of ADPE (17%) was enough to maintain an influent ammonium-nitrogen$({\rm NH}_{4}{}^{+}\text{-}{\rm N})$concentration of 0.17 to 0.19 kg${\rm NH}_{4}{}^{+}\text{-}{\rm N}/{\rm m}^{3}$, which was practically spent.</description><subject>ANAEROBIC DIGESTION</subject><subject>ANAEROBIC FILTER</subject><subject>ANAEROBIC TREATMENT</subject><subject>Applied sciences</subject><subject>Biological and medical sciences</subject><subject>Biological treatment of waters</subject><subject>Biotechnology</subject><subject>Chemical oxygen demand</subject><subject>Environment and pollution</subject><subject>Exact sciences and technology</subject><subject>FACTORIES</subject><subject>FATS</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>GAS PRODUCTION</subject><subject>Industrial applications and implications. 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L</au><au>Martins Dias, S</au><au>Novais, J.M</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Anaerobic treatment of olive mill wastewater with digested piggery effluent</atitle><jtitle>Water environment research</jtitle><date>1998-07</date><risdate>1998</risdate><volume>70</volume><issue>5</issue><spage>1056</spage><epage>1061</epage><pages>1056-1061</pages><issn>1061-4303</issn><eissn>1554-7531</eissn><abstract>Anaerobic digestion of olive mill wastewater (OMW) in admixture with anaerobically digested piggery effluent (ADPE) was investigated. Successive volumetric increases of OMW ranging from 8 to 91% were mixed with ADPE and treated through an upflow anaerobic filter to promote gradual adaptation of the microbial consortium. The response of the digester was positive, and only at 91% v/v OMW was lower reactor performance obtained, suggesting that a concentration on the order of 83% v/v was the highest in terms of the efficiency and stability of the reactor. At this inlet composition, the mixture loading rate varied from 5.0 to 5.7 kg chemical oxygen demand$({\rm COD})/{\rm m}^{3}\cdot {\rm d}$and the total COD removal was 73 to 75%, with a gas production of 1.7 to 2.1${\rm m}^{3}/{\rm m}^{3}\cdot {\rm d}$(66 to 68%${\rm CH}_{4}$). The corresponding volume of ADPE (17%) was enough to maintain an influent ammonium-nitrogen$({\rm NH}_{4}{}^{+}\text{-}{\rm N})$concentration of 0.17 to 0.19 kg${\rm NH}_{4}{}^{+}\text{-}{\rm N}/{\rm m}^{3}$, which was practically spent.</abstract><cop>Alexandria, VA</cop><pub>Water Environment Federation</pub><doi>10.2175/106143098X123390</doi><tpages>6</tpages></addata></record> |
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subjects | ANAEROBIC DIGESTION ANAEROBIC FILTER ANAEROBIC TREATMENT Applied sciences Biological and medical sciences Biological treatment of waters Biotechnology Chemical oxygen demand Environment and pollution Exact sciences and technology FACTORIES FATS Fundamental and applied biological sciences. Psychology GAS PRODUCTION Industrial applications and implications. Economical aspects Industrial effluents Industrial wastewaters Loading rate LOADING RATIO MEASUREMENT Methane METHANE FERMENTATION MIXTURES OILS INDUSTRY OLIVE MILL WASTEWATER OLIVE OIL Pig housing PIGGERIES PIGGERY EFFLUENT POLLUTANT LOAD Pollution REMOVAL Research Papers VOLATILE FATTY ACIDS WASTEWATER WASTEWATER TREATMENT Wastewaters Water treatment and pollution |
title | Anaerobic treatment of olive mill wastewater with digested piggery effluent |
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