Hydrogen production from glucose-containing wastewater using an anaerobic sequencing batch reactor: Effects of COD loading rate, nitrogen content, and organic acid composition
In this work, the process performance of an anaerobic sequencing batch reactor (ASBR) for the hydrogen production from glucose-containing wastewater was studied. The anaerobic sludge taken from a brewery wastewater-treating anaerobic unit was pretreated by boiling for 15 min before being added into...
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| Veröffentlicht in: | Chemical engineering journal (Lausanne, Switzerland : 1996) Switzerland : 1996), 2010-05, Vol.160 (1), p.322-332 |
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| container_title | Chemical engineering journal (Lausanne, Switzerland : 1996) |
| container_volume | 160 |
| creator | Sreethawong, Thammanoon Niyamapa, Tharathip Neramitsuk, Hannarong Rangsunvigit, Pramoch Leethochawalit, Malinee Chavadej, Sumaeth |
| description | In this work, the process performance of an anaerobic sequencing batch reactor (ASBR) for the hydrogen production from glucose-containing wastewater was studied. The anaerobic sludge taken from a brewery wastewater-treating anaerobic unit was pretreated by boiling for 15
min before being added into the ASBR unit as the seeding sludge. The ASBR unit was operated at a temperature of 37
°C, a hydraulic reaction time (HRT) of 24
h, and different chemical oxygen demand (COD) loading rates from 10 to 50
kg
m
−3
d
−1 without and with pH control at 5.5. The results showed that at the optimum COD loading rate of 40
kg
m
−3
d
−1 and pH 5.5, the produced gas was found to contain 44% H
2 and 56% CO
2, and no methane in the produced gas was detected at all operating conditions. At these optimum conditions, the highest hydrogen yield was 1.46
mol H
2/mol glucose consumed. Additionally, the main organic components in the liquid effluent were acetic and butyric acids. Under the optimum COD-to-nitrogen (COD:N) ratio of 100:2.4, the system with pH controlled at 5.5 gave the highest specific H
2 production rate of 7.44
l
H
2
l
−1
d
−1, corresponding to the highest butyric acid to acetic acid ratio. |
| doi_str_mv | 10.1016/j.cej.2010.03.037 |
| format | Article |
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min before being added into the ASBR unit as the seeding sludge. The ASBR unit was operated at a temperature of 37
°C, a hydraulic reaction time (HRT) of 24
h, and different chemical oxygen demand (COD) loading rates from 10 to 50
kg
m
−3
d
−1 without and with pH control at 5.5. The results showed that at the optimum COD loading rate of 40
kg
m
−3
d
−1 and pH 5.5, the produced gas was found to contain 44% H
2 and 56% CO
2, and no methane in the produced gas was detected at all operating conditions. At these optimum conditions, the highest hydrogen yield was 1.46
mol H
2/mol glucose consumed. Additionally, the main organic components in the liquid effluent were acetic and butyric acids. Under the optimum COD-to-nitrogen (COD:N) ratio of 100:2.4, the system with pH controlled at 5.5 gave the highest specific H
2 production rate of 7.44
l
H
2
l
−1
d
−1, corresponding to the highest butyric acid to acetic acid ratio.</description><identifier>ISSN: 1385-8947</identifier><identifier>EISSN: 1873-3212</identifier><identifier>DOI: 10.1016/j.cej.2010.03.037</identifier><language>eng</language><publisher>Oxford: Elsevier B.V</publisher><subject>Anaerobic sequencing batch reactor ; Applied sciences ; Biological and medical sciences ; Biotechnology ; Butyric acid ; Chemical engineering ; COD loading rate ; COD:N ratio ; Crack opening displacement ; Exact sciences and technology ; Fundamental and applied biological sciences. Psychology ; General purification processes ; Glucose ; Hydrogen production ; Loading rate ; Methods. Procedures. Technologies ; Optimization ; Others ; Pollution ; Reactors ; Sequencing ; Sludge ; Various methods and equipments ; Waste water ; Wastewaters ; Water treatment and pollution</subject><ispartof>Chemical engineering journal (Lausanne, Switzerland : 1996), 2010-05, Vol.160 (1), p.322-332</ispartof><rights>2010 Elsevier B.V.</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c425t-52d05a10625dc7fdd31e28a49cbcd8bde76120d31f0bd52efb530c20d1c96c733</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.cej.2010.03.037$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3548,27923,27924,45994</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=22757910$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Sreethawong, Thammanoon</creatorcontrib><creatorcontrib>Niyamapa, Tharathip</creatorcontrib><creatorcontrib>Neramitsuk, Hannarong</creatorcontrib><creatorcontrib>Rangsunvigit, Pramoch</creatorcontrib><creatorcontrib>Leethochawalit, Malinee</creatorcontrib><creatorcontrib>Chavadej, Sumaeth</creatorcontrib><title>Hydrogen production from glucose-containing wastewater using an anaerobic sequencing batch reactor: Effects of COD loading rate, nitrogen content, and organic acid composition</title><title>Chemical engineering journal (Lausanne, Switzerland : 1996)</title><description>In this work, the process performance of an anaerobic sequencing batch reactor (ASBR) for the hydrogen production from glucose-containing wastewater was studied. The anaerobic sludge taken from a brewery wastewater-treating anaerobic unit was pretreated by boiling for 15
min before being added into the ASBR unit as the seeding sludge. The ASBR unit was operated at a temperature of 37
°C, a hydraulic reaction time (HRT) of 24
h, and different chemical oxygen demand (COD) loading rates from 10 to 50
kg
m
−3
d
−1 without and with pH control at 5.5. The results showed that at the optimum COD loading rate of 40
kg
m
−3
d
−1 and pH 5.5, the produced gas was found to contain 44% H
2 and 56% CO
2, and no methane in the produced gas was detected at all operating conditions. At these optimum conditions, the highest hydrogen yield was 1.46
mol H
2/mol glucose consumed. Additionally, the main organic components in the liquid effluent were acetic and butyric acids. Under the optimum COD-to-nitrogen (COD:N) ratio of 100:2.4, the system with pH controlled at 5.5 gave the highest specific H
2 production rate of 7.44
l
H
2
l
−1
d
−1, corresponding to the highest butyric acid to acetic acid ratio.</description><subject>Anaerobic sequencing batch reactor</subject><subject>Applied sciences</subject><subject>Biological and medical sciences</subject><subject>Biotechnology</subject><subject>Butyric acid</subject><subject>Chemical engineering</subject><subject>COD loading rate</subject><subject>COD:N ratio</subject><subject>Crack opening displacement</subject><subject>Exact sciences and technology</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>General purification processes</subject><subject>Glucose</subject><subject>Hydrogen production</subject><subject>Loading rate</subject><subject>Methods. Procedures. Technologies</subject><subject>Optimization</subject><subject>Others</subject><subject>Pollution</subject><subject>Reactors</subject><subject>Sequencing</subject><subject>Sludge</subject><subject>Various methods and equipments</subject><subject>Waste water</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>1385-8947</issn><issn>1873-3212</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2010</creationdate><recordtype>article</recordtype><recordid>eNp9UU1v1DAQjRBIlMIP4OYL4tIs_tjECZzQUihSpV7gbDnj8eJV1l5sp1V_FX-RibbiiDSS7ec3b2beNM1bwTeCi_7DYQN42EhOb64o9LPmQgxatUoK-ZzuaujaYdzql82rUg6c834U40Xz5-bR5bTHyE45uQVqSJH5nI5sPy-QCraQYrUhhrhnD7ZUfLAVM1vKCthIYTGnKQAr-HvBCCs-2Qq_WEYLNeWP7Np7hFpY8mx394XNybqVlUnpisVQzw2shTDWK5J0LOW9jSRqITj6OZ5SCWtvr5sX3s4F3zydl83Pr9c_djft7d2377vPty1sZVfbTjreWcF72TnQ3jklUA52O8IEbpgc6l5ITqjnk-sk-qlTHAgRMPaglbps3p91yRYaq1RzDAVwnm3EtBSjt92o-Dj0xBRnJuRUSkZvTjkcbX40gpt1N-ZgaDdm3Y3hikJTzrsndVvAzj5b8q38S5RSd3oUnHifzjykUe8DZlMgkMfoQiZHjUvhP1X-AkWMqI8</recordid><startdate>20100515</startdate><enddate>20100515</enddate><creator>Sreethawong, Thammanoon</creator><creator>Niyamapa, Tharathip</creator><creator>Neramitsuk, Hannarong</creator><creator>Rangsunvigit, Pramoch</creator><creator>Leethochawalit, Malinee</creator><creator>Chavadej, Sumaeth</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>7SU</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>JG9</scope></search><sort><creationdate>20100515</creationdate><title>Hydrogen production from glucose-containing wastewater using an anaerobic sequencing batch reactor: Effects of COD loading rate, nitrogen content, and organic acid composition</title><author>Sreethawong, Thammanoon ; Niyamapa, Tharathip ; Neramitsuk, Hannarong ; Rangsunvigit, Pramoch ; Leethochawalit, Malinee ; Chavadej, Sumaeth</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c425t-52d05a10625dc7fdd31e28a49cbcd8bde76120d31f0bd52efb530c20d1c96c733</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2010</creationdate><topic>Anaerobic sequencing batch reactor</topic><topic>Applied sciences</topic><topic>Biological and medical sciences</topic><topic>Biotechnology</topic><topic>Butyric acid</topic><topic>Chemical engineering</topic><topic>COD loading rate</topic><topic>COD:N ratio</topic><topic>Crack opening displacement</topic><topic>Exact sciences and technology</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>General purification processes</topic><topic>Glucose</topic><topic>Hydrogen production</topic><topic>Loading rate</topic><topic>Methods. Procedures. Technologies</topic><topic>Optimization</topic><topic>Others</topic><topic>Pollution</topic><topic>Reactors</topic><topic>Sequencing</topic><topic>Sludge</topic><topic>Various methods and equipments</topic><topic>Waste water</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Sreethawong, Thammanoon</creatorcontrib><creatorcontrib>Niyamapa, Tharathip</creatorcontrib><creatorcontrib>Neramitsuk, Hannarong</creatorcontrib><creatorcontrib>Rangsunvigit, Pramoch</creatorcontrib><creatorcontrib>Leethochawalit, Malinee</creatorcontrib><creatorcontrib>Chavadej, Sumaeth</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Environmental Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Materials Research Database</collection><jtitle>Chemical engineering journal (Lausanne, Switzerland : 1996)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Sreethawong, Thammanoon</au><au>Niyamapa, Tharathip</au><au>Neramitsuk, Hannarong</au><au>Rangsunvigit, Pramoch</au><au>Leethochawalit, Malinee</au><au>Chavadej, Sumaeth</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Hydrogen production from glucose-containing wastewater using an anaerobic sequencing batch reactor: Effects of COD loading rate, nitrogen content, and organic acid composition</atitle><jtitle>Chemical engineering journal (Lausanne, Switzerland : 1996)</jtitle><date>2010-05-15</date><risdate>2010</risdate><volume>160</volume><issue>1</issue><spage>322</spage><epage>332</epage><pages>322-332</pages><issn>1385-8947</issn><eissn>1873-3212</eissn><abstract>In this work, the process performance of an anaerobic sequencing batch reactor (ASBR) for the hydrogen production from glucose-containing wastewater was studied. The anaerobic sludge taken from a brewery wastewater-treating anaerobic unit was pretreated by boiling for 15
min before being added into the ASBR unit as the seeding sludge. The ASBR unit was operated at a temperature of 37
°C, a hydraulic reaction time (HRT) of 24
h, and different chemical oxygen demand (COD) loading rates from 10 to 50
kg
m
−3
d
−1 without and with pH control at 5.5. The results showed that at the optimum COD loading rate of 40
kg
m
−3
d
−1 and pH 5.5, the produced gas was found to contain 44% H
2 and 56% CO
2, and no methane in the produced gas was detected at all operating conditions. At these optimum conditions, the highest hydrogen yield was 1.46
mol H
2/mol glucose consumed. Additionally, the main organic components in the liquid effluent were acetic and butyric acids. Under the optimum COD-to-nitrogen (COD:N) ratio of 100:2.4, the system with pH controlled at 5.5 gave the highest specific H
2 production rate of 7.44
l
H
2
l
−1
d
−1, corresponding to the highest butyric acid to acetic acid ratio.</abstract><cop>Oxford</cop><pub>Elsevier B.V</pub><doi>10.1016/j.cej.2010.03.037</doi><tpages>11</tpages></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 1385-8947 |
| ispartof | Chemical engineering journal (Lausanne, Switzerland : 1996), 2010-05, Vol.160 (1), p.322-332 |
| issn | 1385-8947 1873-3212 |
| language | eng |
| recordid | cdi_proquest_miscellaneous_745930986 |
| source | ScienceDirect Journals (5 years ago - present) |
| subjects | Anaerobic sequencing batch reactor Applied sciences Biological and medical sciences Biotechnology Butyric acid Chemical engineering COD loading rate COD:N ratio Crack opening displacement Exact sciences and technology Fundamental and applied biological sciences. Psychology General purification processes Glucose Hydrogen production Loading rate Methods. Procedures. Technologies Optimization Others Pollution Reactors Sequencing Sludge Various methods and equipments Waste water Wastewaters Water treatment and pollution |
| title | Hydrogen production from glucose-containing wastewater using an anaerobic sequencing batch reactor: Effects of COD loading rate, nitrogen content, and organic acid composition |
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