Experimental investigation of acid regeneration of spent bleaching clay de-oiled by the in-situ transesterification process at various operating conditions
[Display omitted] •In-situ transesterification of SBC was performed to de-oil the clay.•Regeneration of the SBC was performed by the conventional acid activating process.•The effect of transesterification were investigated on the regenerating efficiency.•Lower energy required than the other regenera...
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Veröffentlicht in: | Process safety and environmental protection 2019-04, Vol.124, p.121-127 |
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creator | Sedghamiz, M.A. Attar, F. Raeissi, S. |
description | [Display omitted]
•In-situ transesterification of SBC was performed to de-oil the clay.•Regeneration of the SBC was performed by the conventional acid activating process.•The effect of transesterification were investigated on the regenerating efficiency.•Lower energy required than the other regeneration methods, e.g. heat treatment.
The spent bleaching clay (SBC) from the edible oil refining industries contains different types of contaminants, including fatty acids and trace amounts of heavy metals and hazardous materials. Therefore, the conventional procedure of landfilling of SBC is not safe for the environment. Because of this, researchers have been trying to find alternative routes, such as novel processes to regenerate the clay and reuse it. The large amounts of oil remaining in SBC justifies the investigation of in-situ transesterification of the oil to biodiesel. In this study, clays that have been de-oiled by in-situ transesterification at various operating conditions are investigated for their final regenerated bleaching capacity. The different in-situ operating parameters considered are: the choice between two different alkali catalysts, catalyst/SBC ratio, ethanol/SBC ratio, temperature, and reaction time. With 60 different experiments and using the method of experimental design, the optimum operating parameters were determined and presented for achieving maximum bleaching capacity of the regenerated clay. The suggested conditions were then confirmed experimentally. Results showed that the maximum bleaching capacity at these optimum conditions was 17.03%. |
doi_str_mv | 10.1016/j.psep.2019.01.029 |
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•In-situ transesterification of SBC was performed to de-oil the clay.•Regeneration of the SBC was performed by the conventional acid activating process.•The effect of transesterification were investigated on the regenerating efficiency.•Lower energy required than the other regeneration methods, e.g. heat treatment.
The spent bleaching clay (SBC) from the edible oil refining industries contains different types of contaminants, including fatty acids and trace amounts of heavy metals and hazardous materials. Therefore, the conventional procedure of landfilling of SBC is not safe for the environment. Because of this, researchers have been trying to find alternative routes, such as novel processes to regenerate the clay and reuse it. The large amounts of oil remaining in SBC justifies the investigation of in-situ transesterification of the oil to biodiesel. In this study, clays that have been de-oiled by in-situ transesterification at various operating conditions are investigated for their final regenerated bleaching capacity. The different in-situ operating parameters considered are: the choice between two different alkali catalysts, catalyst/SBC ratio, ethanol/SBC ratio, temperature, and reaction time. With 60 different experiments and using the method of experimental design, the optimum operating parameters were determined and presented for achieving maximum bleaching capacity of the regenerated clay. The suggested conditions were then confirmed experimentally. Results showed that the maximum bleaching capacity at these optimum conditions was 17.03%.</description><identifier>ISSN: 0957-5820</identifier><identifier>EISSN: 1744-3598</identifier><identifier>DOI: 10.1016/j.psep.2019.01.029</identifier><language>eng</language><publisher>Rugby: Elsevier B.V</publisher><subject>Acid activating ; Biodiesel fuels ; Biofuels ; Bleaching ; Bleaching capacity ; Bleaching earth ; Catalysis ; Catalysts ; Clay ; Contaminants ; Design of experiments ; Design parameters ; Edible oils ; Ethanol ; Experimental design ; Fatty acids ; Hazardous materials ; Heavy metals ; In-situ esterification ; Landfills ; Oil ; Petroleum refining ; Reaction time ; Regeneration ; Spent bleaching clay ; Trace metals ; Transesterification</subject><ispartof>Process safety and environmental protection, 2019-04, Vol.124, p.121-127</ispartof><rights>2019</rights><rights>Copyright Elsevier Science Ltd. Apr 2019</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c365t-3323a80c2c4acddfd4b1304099df69da347dd18b17a6c6714683fdcb112679633</citedby><cites>FETCH-LOGICAL-c365t-3323a80c2c4acddfd4b1304099df69da347dd18b17a6c6714683fdcb112679633</cites><orcidid>0000-0002-7383-3172</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.psep.2019.01.029$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3549,27923,27924,45994</link.rule.ids></links><search><creatorcontrib>Sedghamiz, M.A.</creatorcontrib><creatorcontrib>Attar, F.</creatorcontrib><creatorcontrib>Raeissi, S.</creatorcontrib><title>Experimental investigation of acid regeneration of spent bleaching clay de-oiled by the in-situ transesterification process at various operating conditions</title><title>Process safety and environmental protection</title><description>[Display omitted]
•In-situ transesterification of SBC was performed to de-oil the clay.•Regeneration of the SBC was performed by the conventional acid activating process.•The effect of transesterification were investigated on the regenerating efficiency.•Lower energy required than the other regeneration methods, e.g. heat treatment.
The spent bleaching clay (SBC) from the edible oil refining industries contains different types of contaminants, including fatty acids and trace amounts of heavy metals and hazardous materials. Therefore, the conventional procedure of landfilling of SBC is not safe for the environment. Because of this, researchers have been trying to find alternative routes, such as novel processes to regenerate the clay and reuse it. The large amounts of oil remaining in SBC justifies the investigation of in-situ transesterification of the oil to biodiesel. In this study, clays that have been de-oiled by in-situ transesterification at various operating conditions are investigated for their final regenerated bleaching capacity. The different in-situ operating parameters considered are: the choice between two different alkali catalysts, catalyst/SBC ratio, ethanol/SBC ratio, temperature, and reaction time. With 60 different experiments and using the method of experimental design, the optimum operating parameters were determined and presented for achieving maximum bleaching capacity of the regenerated clay. The suggested conditions were then confirmed experimentally. Results showed that the maximum bleaching capacity at these optimum conditions was 17.03%.</description><subject>Acid activating</subject><subject>Biodiesel fuels</subject><subject>Biofuels</subject><subject>Bleaching</subject><subject>Bleaching capacity</subject><subject>Bleaching earth</subject><subject>Catalysis</subject><subject>Catalysts</subject><subject>Clay</subject><subject>Contaminants</subject><subject>Design of experiments</subject><subject>Design parameters</subject><subject>Edible oils</subject><subject>Ethanol</subject><subject>Experimental design</subject><subject>Fatty acids</subject><subject>Hazardous materials</subject><subject>Heavy metals</subject><subject>In-situ esterification</subject><subject>Landfills</subject><subject>Oil</subject><subject>Petroleum refining</subject><subject>Reaction time</subject><subject>Regeneration</subject><subject>Spent bleaching clay</subject><subject>Trace metals</subject><subject>Transesterification</subject><issn>0957-5820</issn><issn>1744-3598</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNp9kc1q4zAUhcXQgUkz8wKzEnRtV1dy_APdlNI_KHTTroUsXScKHsmVlNA8S1925KR02ZVAnPOdwz2E_AVWAoP6cltOEaeSM-hKBiXj3Q-ygKaqCrHq2jOyYN2qKVYtZ7_IeYxbxhjwBhbk4_Z9wmD_oUtqpNbtMSa7Vsl6R_1AlbaGBlyjw_D1Gaespv2ISm-sW1M9qgM1WHg7oqH9gaYNZlQRbdrRFJSLGZpDBqtPjCl4jTFSleheBet3kfrpGDDTvDN2lsXf5Oegxoh_Pt8leb27fbl5KJ6e7x9vrp8KLepVKoTgQrVMc10pbcxgqh4Eq1jXmaHujBJVYwy0PTSq1nUDVd2KwegegNdNVwuxJBcnbu71tstd5dbvgsuRknNoBQNxVPGTSgcfY8BBTvluKhwkMDmPILdyHkHOI0gGMo-QTVcnE-b-e4tBRm3RaTQ2oE7SePud_T_AJZSR</recordid><startdate>20190401</startdate><enddate>20190401</enddate><creator>Sedghamiz, M.A.</creator><creator>Attar, F.</creator><creator>Raeissi, S.</creator><general>Elsevier B.V</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7TB</scope><scope>7U7</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>KR7</scope><scope>SOI</scope><orcidid>https://orcid.org/0000-0002-7383-3172</orcidid></search><sort><creationdate>20190401</creationdate><title>Experimental investigation of acid regeneration of spent bleaching clay de-oiled by the in-situ transesterification process at various operating conditions</title><author>Sedghamiz, M.A. ; Attar, F. ; Raeissi, S.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c365t-3323a80c2c4acddfd4b1304099df69da347dd18b17a6c6714683fdcb112679633</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>Acid activating</topic><topic>Biodiesel fuels</topic><topic>Biofuels</topic><topic>Bleaching</topic><topic>Bleaching capacity</topic><topic>Bleaching earth</topic><topic>Catalysis</topic><topic>Catalysts</topic><topic>Clay</topic><topic>Contaminants</topic><topic>Design of experiments</topic><topic>Design parameters</topic><topic>Edible oils</topic><topic>Ethanol</topic><topic>Experimental design</topic><topic>Fatty acids</topic><topic>Hazardous materials</topic><topic>Heavy metals</topic><topic>In-situ esterification</topic><topic>Landfills</topic><topic>Oil</topic><topic>Petroleum refining</topic><topic>Reaction time</topic><topic>Regeneration</topic><topic>Spent bleaching clay</topic><topic>Trace metals</topic><topic>Transesterification</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Sedghamiz, M.A.</creatorcontrib><creatorcontrib>Attar, F.</creatorcontrib><creatorcontrib>Raeissi, S.</creatorcontrib><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Toxicology Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>Environment Abstracts</collection><jtitle>Process safety and environmental protection</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Sedghamiz, M.A.</au><au>Attar, F.</au><au>Raeissi, S.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Experimental investigation of acid regeneration of spent bleaching clay de-oiled by the in-situ transesterification process at various operating conditions</atitle><jtitle>Process safety and environmental protection</jtitle><date>2019-04-01</date><risdate>2019</risdate><volume>124</volume><spage>121</spage><epage>127</epage><pages>121-127</pages><issn>0957-5820</issn><eissn>1744-3598</eissn><abstract>[Display omitted]
•In-situ transesterification of SBC was performed to de-oil the clay.•Regeneration of the SBC was performed by the conventional acid activating process.•The effect of transesterification were investigated on the regenerating efficiency.•Lower energy required than the other regeneration methods, e.g. heat treatment.
The spent bleaching clay (SBC) from the edible oil refining industries contains different types of contaminants, including fatty acids and trace amounts of heavy metals and hazardous materials. Therefore, the conventional procedure of landfilling of SBC is not safe for the environment. Because of this, researchers have been trying to find alternative routes, such as novel processes to regenerate the clay and reuse it. The large amounts of oil remaining in SBC justifies the investigation of in-situ transesterification of the oil to biodiesel. In this study, clays that have been de-oiled by in-situ transesterification at various operating conditions are investigated for their final regenerated bleaching capacity. The different in-situ operating parameters considered are: the choice between two different alkali catalysts, catalyst/SBC ratio, ethanol/SBC ratio, temperature, and reaction time. With 60 different experiments and using the method of experimental design, the optimum operating parameters were determined and presented for achieving maximum bleaching capacity of the regenerated clay. The suggested conditions were then confirmed experimentally. Results showed that the maximum bleaching capacity at these optimum conditions was 17.03%.</abstract><cop>Rugby</cop><pub>Elsevier B.V</pub><doi>10.1016/j.psep.2019.01.029</doi><tpages>7</tpages><orcidid>https://orcid.org/0000-0002-7383-3172</orcidid></addata></record> |
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source | ScienceDirect Journals (5 years ago - present) |
subjects | Acid activating Biodiesel fuels Biofuels Bleaching Bleaching capacity Bleaching earth Catalysis Catalysts Clay Contaminants Design of experiments Design parameters Edible oils Ethanol Experimental design Fatty acids Hazardous materials Heavy metals In-situ esterification Landfills Oil Petroleum refining Reaction time Regeneration Spent bleaching clay Trace metals Transesterification |
title | Experimental investigation of acid regeneration of spent bleaching clay de-oiled by the in-situ transesterification process at various operating conditions |
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