Technical and economic potential of high-temperature NF and DCMD for gold mining effluent reclamation
[Display omitted] •The performance of high-temperature NF and DCMD was compared•DCMD showed better physical chemical quality compared to NF•The energy cost related to DCMD was significantly lower (99.47%) compared to NF Direct contact membrane distillation (DCMD) and high-temperature nanofiltration...
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Veröffentlicht in: | Chemical engineering research & design 2020-10, Vol.162, p.149-161 |
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creator | Foureaux, A.F.S. Lebron, Y.A.R. Moreira, V.R. Grossi, L.B. Santos, L.V.S. Amaral, M.C.S. |
description | [Display omitted]
•The performance of high-temperature NF and DCMD was compared•DCMD showed better physical chemical quality compared to NF•The energy cost related to DCMD was significantly lower (99.47%) compared to NF
Direct contact membrane distillation (DCMD) and high-temperature nanofiltration (NF) were compared in terms of technical and economic aspects for the treatment of pressure oxidation process (POX) real effluent. Tests were carried out in bench scale and differences in fouling behavior and its impacts on NF and MD performance were evaluated. High pollutants rejection rates were observed for both systems (>92.4 %). However, DCMD had better permeate quality and lower energy requirement, which contributed significantly to its lower operational costs due to use of the effluent residual heat. CAPEX and OPEX were estimated at US$/m3 2.251 for NF and US$/m3 0.233 for DCMD. DCMD application represents a saving of US$ 45,138.3 annually supplying 250,768.3 m3 of high-quality reuse water. At the end, this research allowed for a better comprehension of these membrane technologies, preventing the production of waste and increasing efficiencies in the uses of energy, water, and resources. |
doi_str_mv | 10.1016/j.cherd.2020.08.003 |
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•The performance of high-temperature NF and DCMD was compared•DCMD showed better physical chemical quality compared to NF•The energy cost related to DCMD was significantly lower (99.47%) compared to NF
Direct contact membrane distillation (DCMD) and high-temperature nanofiltration (NF) were compared in terms of technical and economic aspects for the treatment of pressure oxidation process (POX) real effluent. Tests were carried out in bench scale and differences in fouling behavior and its impacts on NF and MD performance were evaluated. High pollutants rejection rates were observed for both systems (>92.4 %). However, DCMD had better permeate quality and lower energy requirement, which contributed significantly to its lower operational costs due to use of the effluent residual heat. CAPEX and OPEX were estimated at US$/m3 2.251 for NF and US$/m3 0.233 for DCMD. DCMD application represents a saving of US$ 45,138.3 annually supplying 250,768.3 m3 of high-quality reuse water. At the end, this research allowed for a better comprehension of these membrane technologies, preventing the production of waste and increasing efficiencies in the uses of energy, water, and resources.</description><identifier>ISSN: 0263-8762</identifier><identifier>EISSN: 1744-3563</identifier><identifier>DOI: 10.1016/j.cherd.2020.08.003</identifier><language>eng</language><publisher>Rugby: Elsevier B.V</publisher><subject>Acid solution ; Distillation ; Effluents ; Heat transfer ; High temperature ; Membrane distillation ; Membranes ; Metals ; Mine reclamation ; Nanofiltration ; Oxidation ; Pollutants ; Pollution control ; Rejection rate ; Reuse water ; Water quality ; Water reuse</subject><ispartof>Chemical engineering research & design, 2020-10, Vol.162, p.149-161</ispartof><rights>2020 Institution of Chemical Engineers</rights><rights>Copyright Elsevier Science Ltd. Oct 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c331t-7c53c0d61742e925bbb5553b4294d8fba223e0dfb93a011000a6222d012382563</citedby><cites>FETCH-LOGICAL-c331t-7c53c0d61742e925bbb5553b4294d8fba223e0dfb93a011000a6222d012382563</cites><orcidid>0000-0001-6368-3310 ; 0000-0001-6933-8454</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0263876220303506$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65534</link.rule.ids></links><search><creatorcontrib>Foureaux, A.F.S.</creatorcontrib><creatorcontrib>Lebron, Y.A.R.</creatorcontrib><creatorcontrib>Moreira, V.R.</creatorcontrib><creatorcontrib>Grossi, L.B.</creatorcontrib><creatorcontrib>Santos, L.V.S.</creatorcontrib><creatorcontrib>Amaral, M.C.S.</creatorcontrib><title>Technical and economic potential of high-temperature NF and DCMD for gold mining effluent reclamation</title><title>Chemical engineering research & design</title><description>[Display omitted]
•The performance of high-temperature NF and DCMD was compared•DCMD showed better physical chemical quality compared to NF•The energy cost related to DCMD was significantly lower (99.47%) compared to NF
Direct contact membrane distillation (DCMD) and high-temperature nanofiltration (NF) were compared in terms of technical and economic aspects for the treatment of pressure oxidation process (POX) real effluent. Tests were carried out in bench scale and differences in fouling behavior and its impacts on NF and MD performance were evaluated. High pollutants rejection rates were observed for both systems (>92.4 %). However, DCMD had better permeate quality and lower energy requirement, which contributed significantly to its lower operational costs due to use of the effluent residual heat. CAPEX and OPEX were estimated at US$/m3 2.251 for NF and US$/m3 0.233 for DCMD. DCMD application represents a saving of US$ 45,138.3 annually supplying 250,768.3 m3 of high-quality reuse water. At the end, this research allowed for a better comprehension of these membrane technologies, preventing the production of waste and increasing efficiencies in the uses of energy, water, and resources.</description><subject>Acid solution</subject><subject>Distillation</subject><subject>Effluents</subject><subject>Heat transfer</subject><subject>High temperature</subject><subject>Membrane distillation</subject><subject>Membranes</subject><subject>Metals</subject><subject>Mine reclamation</subject><subject>Nanofiltration</subject><subject>Oxidation</subject><subject>Pollutants</subject><subject>Pollution control</subject><subject>Rejection rate</subject><subject>Reuse water</subject><subject>Water quality</subject><subject>Water reuse</subject><issn>0263-8762</issn><issn>1744-3563</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9kE9PwzAMxSMEEmPwCbhE4tziJP23Awe0MUAacBnnKE3cLVWbjLRD4tuTbZw5WbLfs_17hNwySBmw4r5N9RaDSTlwSKFKAcQZmbAyyxKRF-KcTIAXIqnKgl-Sq2FoASBOqwnBNeqts1p1VDlDUXvne6vpzo_oRhvbvqFbu9kmI_Y7DGrcB6Tvy6N6MX9b0MYHuvGdob111m0oNk23j14aUHeqV6P17ppcNKob8OavTsnn8mk9f0lWH8-v88dVooVgY1LqXGgwRXyN44zndV3neS7qjM8yUzW14lwgmKaeCQWMRQhVcM4NMC4qHkGn5O60dxf81x6HUbZ-H1w8KXlWzrKKFaKKKnFS6eCHIWAjd8H2KvxIBvKQp2zlMU95yFNCJWOe0fVwcmEE-LYY5KAtOo3GRtJRGm__9f8ChJV-Lw</recordid><startdate>202010</startdate><enddate>202010</enddate><creator>Foureaux, A.F.S.</creator><creator>Lebron, Y.A.R.</creator><creator>Moreira, V.R.</creator><creator>Grossi, L.B.</creator><creator>Santos, L.V.S.</creator><creator>Amaral, M.C.S.</creator><general>Elsevier B.V</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7SR</scope><scope>8FD</scope><scope>JG9</scope><orcidid>https://orcid.org/0000-0001-6368-3310</orcidid><orcidid>https://orcid.org/0000-0001-6933-8454</orcidid></search><sort><creationdate>202010</creationdate><title>Technical and economic potential of high-temperature NF and DCMD for gold mining effluent reclamation</title><author>Foureaux, A.F.S. ; Lebron, Y.A.R. ; Moreira, V.R. ; Grossi, L.B. ; Santos, L.V.S. ; Amaral, M.C.S.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c331t-7c53c0d61742e925bbb5553b4294d8fba223e0dfb93a011000a6222d012382563</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Acid solution</topic><topic>Distillation</topic><topic>Effluents</topic><topic>Heat transfer</topic><topic>High temperature</topic><topic>Membrane distillation</topic><topic>Membranes</topic><topic>Metals</topic><topic>Mine reclamation</topic><topic>Nanofiltration</topic><topic>Oxidation</topic><topic>Pollutants</topic><topic>Pollution control</topic><topic>Rejection rate</topic><topic>Reuse water</topic><topic>Water quality</topic><topic>Water reuse</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Foureaux, A.F.S.</creatorcontrib><creatorcontrib>Lebron, Y.A.R.</creatorcontrib><creatorcontrib>Moreira, V.R.</creatorcontrib><creatorcontrib>Grossi, L.B.</creatorcontrib><creatorcontrib>Santos, L.V.S.</creatorcontrib><creatorcontrib>Amaral, M.C.S.</creatorcontrib><collection>CrossRef</collection><collection>Engineered Materials Abstracts</collection><collection>Technology Research Database</collection><collection>Materials Research Database</collection><jtitle>Chemical engineering research & design</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Foureaux, A.F.S.</au><au>Lebron, Y.A.R.</au><au>Moreira, V.R.</au><au>Grossi, L.B.</au><au>Santos, L.V.S.</au><au>Amaral, M.C.S.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Technical and economic potential of high-temperature NF and DCMD for gold mining effluent reclamation</atitle><jtitle>Chemical engineering research & design</jtitle><date>2020-10</date><risdate>2020</risdate><volume>162</volume><spage>149</spage><epage>161</epage><pages>149-161</pages><issn>0263-8762</issn><eissn>1744-3563</eissn><abstract>[Display omitted]
•The performance of high-temperature NF and DCMD was compared•DCMD showed better physical chemical quality compared to NF•The energy cost related to DCMD was significantly lower (99.47%) compared to NF
Direct contact membrane distillation (DCMD) and high-temperature nanofiltration (NF) were compared in terms of technical and economic aspects for the treatment of pressure oxidation process (POX) real effluent. Tests were carried out in bench scale and differences in fouling behavior and its impacts on NF and MD performance were evaluated. High pollutants rejection rates were observed for both systems (>92.4 %). However, DCMD had better permeate quality and lower energy requirement, which contributed significantly to its lower operational costs due to use of the effluent residual heat. CAPEX and OPEX were estimated at US$/m3 2.251 for NF and US$/m3 0.233 for DCMD. DCMD application represents a saving of US$ 45,138.3 annually supplying 250,768.3 m3 of high-quality reuse water. At the end, this research allowed for a better comprehension of these membrane technologies, preventing the production of waste and increasing efficiencies in the uses of energy, water, and resources.</abstract><cop>Rugby</cop><pub>Elsevier B.V</pub><doi>10.1016/j.cherd.2020.08.003</doi><tpages>13</tpages><orcidid>https://orcid.org/0000-0001-6368-3310</orcidid><orcidid>https://orcid.org/0000-0001-6933-8454</orcidid></addata></record> |
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subjects | Acid solution Distillation Effluents Heat transfer High temperature Membrane distillation Membranes Metals Mine reclamation Nanofiltration Oxidation Pollutants Pollution control Rejection rate Reuse water Water quality Water reuse |
title | Technical and economic potential of high-temperature NF and DCMD for gold mining effluent reclamation |
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