Treatment of an industrial effluent by reverse osmosis
The treatment of tanning wastewater was studied by means of reverse osmosis and ultrafiltration. Tests were carried out on laboratory scale using membranes of polyamide (reverse osmosis) and of polysulfone (ultrafiltration). The evaluation of the system was performed by chemical analysis, pH measure...
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Veröffentlicht in: | Desalination 1999-11, Vol.126 (1), p.219-226 |
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description | The treatment of tanning wastewater was studied by means of reverse osmosis and ultrafiltration. Tests were carried out on laboratory scale using membranes of polyamide (reverse osmosis) and of polysulfone (ultrafiltration). The evaluation of the system was performed by chemical analysis, pH measurements and visible spectrophotometry. Effects of the protein contained in the industrial effluent, the applied pressure and the feed temperature on the permeate flux were analyzed. The polyamide membrane used allowed us to obtain permeates with a low chromium (III) content (7–10 mg/L) but with appreciable amounts of SO
4
= (1–3 g/l), Cl
− (9–14 g/L) and Na
+ (5–10 g/L). The presence of chromium (III) polymers was determined in the original effluent and in the concentrates obtained by reverse osmosis. Finally, it was established that during the operation of reverse osmosis, the transport of H
+(H
3O
+) from the concentrate to the permeate was produced. |
doi_str_mv | 10.1016/S0011-9164(99)00178-2 |
format | Article |
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4
= (1–3 g/l), Cl
− (9–14 g/L) and Na
+ (5–10 g/L). The presence of chromium (III) polymers was determined in the original effluent and in the concentrates obtained by reverse osmosis. Finally, it was established that during the operation of reverse osmosis, the transport of H
+(H
3O
+) from the concentrate to the permeate was produced.</description><identifier>ISSN: 0011-9164</identifier><identifier>EISSN: 1873-4464</identifier><identifier>DOI: 10.1016/S0011-9164(99)00178-2</identifier><identifier>CODEN: DSLNAH</identifier><language>eng</language><publisher>Amsterdam: Elsevier B.V</publisher><subject>Applied sciences ; Chromium (III) ; Exact sciences and technology ; Industrial wastewaters ; Leather ; Pollution ; Recovery ; Reverse osmosis ; Tanning wastewater ; Ultrafiltration ; Wastewaters ; Water treatment and pollution</subject><ispartof>Desalination, 1999-11, Vol.126 (1), p.219-226</ispartof><rights>1999</rights><rights>2000 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c429t-b34a88be0a4bc181715a318a60f1ae184b61d0a163e36793fd21d3420645144f3</citedby><cites>FETCH-LOGICAL-c429t-b34a88be0a4bc181715a318a60f1ae184b61d0a163e36793fd21d3420645144f3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0011916499001782$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>309,310,314,776,780,785,786,3537,23909,23910,25118,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=1198213$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Padilla, Antonio Pérez</creatorcontrib><creatorcontrib>Tavani, Eduardo L.</creatorcontrib><title>Treatment of an industrial effluent by reverse osmosis</title><title>Desalination</title><description>The treatment of tanning wastewater was studied by means of reverse osmosis and ultrafiltration. Tests were carried out on laboratory scale using membranes of polyamide (reverse osmosis) and of polysulfone (ultrafiltration). The evaluation of the system was performed by chemical analysis, pH measurements and visible spectrophotometry. Effects of the protein contained in the industrial effluent, the applied pressure and the feed temperature on the permeate flux were analyzed. The polyamide membrane used allowed us to obtain permeates with a low chromium (III) content (7–10 mg/L) but with appreciable amounts of SO
4
= (1–3 g/l), Cl
− (9–14 g/L) and Na
+ (5–10 g/L). The presence of chromium (III) polymers was determined in the original effluent and in the concentrates obtained by reverse osmosis. Finally, it was established that during the operation of reverse osmosis, the transport of H
+(H
3O
+) from the concentrate to the permeate was produced.</description><subject>Applied sciences</subject><subject>Chromium (III)</subject><subject>Exact sciences and technology</subject><subject>Industrial wastewaters</subject><subject>Leather</subject><subject>Pollution</subject><subject>Recovery</subject><subject>Reverse osmosis</subject><subject>Tanning wastewater</subject><subject>Ultrafiltration</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0011-9164</issn><issn>1873-4464</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1999</creationdate><recordtype>article</recordtype><recordid>eNqNkMtKAzEUhoMoWKuPIMxCRBejOUkmk6xEijcouLCuQyZzApHpTE2mhb690wu6rKvDz_nOhY-QS6B3QEHef1AKkGuQ4kbr2yGUKmdHZASq5LkQUhyT0S9ySs5S-hoi05yPiJxFtP0c2z7rfGbbLLT1MvUx2CZD75vlplOts4grjAmzLs27FNI5OfG2SXixr2Py-fw0m7zm0_eXt8njNHeC6T6vuLBKVUitqBwoKKGwHJSV1INFUKKSUFMLkiOXpea-ZlBzwagUBQjh-Zhc7_YuYve9xNSbeUgOm8a22C2TYVpzKYH-AyyZEIofBKEsNBRSDWCxA13sUorozSKGuY1rA9RsvJutd7ORarQ2W--GDXNX-wM2Odv4aFsX0t8waMVg88fDDsNB3ypgNMkFbB3WIaLrTd2FA4d-AJvUlMY</recordid><startdate>19991101</startdate><enddate>19991101</enddate><creator>Padilla, Antonio Pérez</creator><creator>Tavani, Eduardo L.</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7TV</scope><scope>7UA</scope><scope>C1K</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope><scope>8BQ</scope><scope>JG9</scope><scope>KR7</scope></search><sort><creationdate>19991101</creationdate><title>Treatment of an industrial effluent by reverse osmosis</title><author>Padilla, Antonio Pérez ; Tavani, Eduardo L.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c429t-b34a88be0a4bc181715a318a60f1ae184b61d0a163e36793fd21d3420645144f3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1999</creationdate><topic>Applied sciences</topic><topic>Chromium (III)</topic><topic>Exact sciences and technology</topic><topic>Industrial wastewaters</topic><topic>Leather</topic><topic>Pollution</topic><topic>Recovery</topic><topic>Reverse osmosis</topic><topic>Tanning wastewater</topic><topic>Ultrafiltration</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Padilla, Antonio Pérez</creatorcontrib><creatorcontrib>Tavani, Eduardo L.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Pollution Abstracts</collection><collection>Water Resources Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><collection>METADEX</collection><collection>Materials Research Database</collection><collection>Civil Engineering Abstracts</collection><jtitle>Desalination</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Padilla, Antonio Pérez</au><au>Tavani, Eduardo L.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Treatment of an industrial effluent by reverse osmosis</atitle><jtitle>Desalination</jtitle><date>1999-11-01</date><risdate>1999</risdate><volume>126</volume><issue>1</issue><spage>219</spage><epage>226</epage><pages>219-226</pages><issn>0011-9164</issn><eissn>1873-4464</eissn><coden>DSLNAH</coden><abstract>The treatment of tanning wastewater was studied by means of reverse osmosis and ultrafiltration. Tests were carried out on laboratory scale using membranes of polyamide (reverse osmosis) and of polysulfone (ultrafiltration). The evaluation of the system was performed by chemical analysis, pH measurements and visible spectrophotometry. Effects of the protein contained in the industrial effluent, the applied pressure and the feed temperature on the permeate flux were analyzed. The polyamide membrane used allowed us to obtain permeates with a low chromium (III) content (7–10 mg/L) but with appreciable amounts of SO
4
= (1–3 g/l), Cl
− (9–14 g/L) and Na
+ (5–10 g/L). The presence of chromium (III) polymers was determined in the original effluent and in the concentrates obtained by reverse osmosis. Finally, it was established that during the operation of reverse osmosis, the transport of H
+(H
3O
+) from the concentrate to the permeate was produced.</abstract><cop>Amsterdam</cop><pub>Elsevier B.V</pub><doi>10.1016/S0011-9164(99)00178-2</doi><tpages>8</tpages></addata></record> |
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source | Elsevier ScienceDirect Journals |
subjects | Applied sciences Chromium (III) Exact sciences and technology Industrial wastewaters Leather Pollution Recovery Reverse osmosis Tanning wastewater Ultrafiltration Wastewaters Water treatment and pollution |
title | Treatment of an industrial effluent by reverse osmosis |
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