METODO PER L'OTTENIMENTO IN CONTINUO DI MAGNESIO,E RELATIVO APPARECCHIO A FLUIDO PASSANTE A PIU' CAMERE
The process and plant include a chamber (a) in which fresh MgCl2 is added to an electrolyte; an electrolyte purificn. chamber (b); a chamber (c) for sepg. Mg from the electrolyte; and a chamber (d) which divides the electrolyte into two streams (I,II). One stream (I) is returned to chamber (a) for e...
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creator | VLADIMIR NIKOLAEVICH DEVYATKIN ILIAS AMALBEKOVICH CHALABAEV ARNOLD VASILIEVICH KOLOMIITSEV IGOR VSEVOLODOVICH ZABELIN MURAT KAZMUKHAMEDOVICH BAIBEKOV VIKTOR GRIGORIEVICH SOROKOUS CHAKEN KUDAIBERGENOVICH MEDEUOV EFIM ALEXANDROVICH KITAIGORODSKY NIKOLAI MIKHAILOVICH ZUEV JURY MIKHAILOVICH RYABUKHIN |
description | The process and plant include a chamber (a) in which fresh MgCl2 is added to an electrolyte; an electrolyte purificn. chamber (b); a chamber (c) for sepg. Mg from the electrolyte; and a chamber (d) which divides the electrolyte into two streams (I,II). One stream (I) is returned to chamber (a) for enrichment with MgCl2; whereas the other (II) is fed through a row of electrolysis cells (e), and is then fed into chamber (c). The ratio of the two streams (I:II) is pref. 0.1-0.4:1. In one pref. plant, the molten salt electrolyte leaving chamber (b) is mixed with molten electrolyte leaving the last electrolysis cell in the inlet channel for chamber (c). The yield of Mg per unit of electrical energy is increased; and the purity of the electrolyte fed into the electrolysis cells is raised. |
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Mg from the electrolyte; and a chamber (d) which divides the electrolyte into two streams (I,II). One stream (I) is returned to chamber (a) for enrichment with MgCl2; whereas the other (II) is fed through a row of electrolysis cells (e), and is then fed into chamber (c). The ratio of the two streams (I:II) is pref. 0.1-0.4:1. In one pref. plant, the molten salt electrolyte leaving chamber (b) is mixed with molten electrolyte leaving the last electrolysis cell in the inlet channel for chamber (c). The yield of Mg per unit of electrical energy is increased; and the purity of the electrolyte fed into the electrolysis cells is raised.</description><edition>3</edition><language>ita</language><subject>APPARATUS THEREFOR ; CHEMISTRY ; ELECTROLYTIC OR ELECTROPHORETIC PROCESSES ; METALLURGY ; PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY ORREFINING OF METALS</subject><creationdate>1981</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19810209&DB=EPODOC&CC=IT&NR=8119612A0$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,780,885,25564,76547</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=19810209&DB=EPODOC&CC=IT&NR=8119612A0$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>VLADIMIR NIKOLAEVICH DEVYATKIN</creatorcontrib><creatorcontrib>ILIAS AMALBEKOVICH CHALABAEV</creatorcontrib><creatorcontrib>ARNOLD VASILIEVICH KOLOMIITSEV</creatorcontrib><creatorcontrib>IGOR VSEVOLODOVICH ZABELIN</creatorcontrib><creatorcontrib>MURAT KAZMUKHAMEDOVICH BAIBEKOV</creatorcontrib><creatorcontrib>VIKTOR GRIGORIEVICH SOROKOUS</creatorcontrib><creatorcontrib>CHAKEN KUDAIBERGENOVICH MEDEUOV</creatorcontrib><creatorcontrib>EFIM ALEXANDROVICH KITAIGORODSKY</creatorcontrib><creatorcontrib>NIKOLAI MIKHAILOVICH ZUEV</creatorcontrib><creatorcontrib>JURY MIKHAILOVICH RYABUKHIN</creatorcontrib><title>METODO PER L'OTTENIMENTO IN CONTINUO DI MAGNESIO,E RELATIVO APPARECCHIO A FLUIDO PASSANTE A PIU' CAMERE</title><description>The process and plant include a chamber (a) in which fresh MgCl2 is added to an electrolyte; an electrolyte purificn. chamber (b); a chamber (c) for sepg. Mg from the electrolyte; and a chamber (d) which divides the electrolyte into two streams (I,II). One stream (I) is returned to chamber (a) for enrichment with MgCl2; whereas the other (II) is fed through a row of electrolysis cells (e), and is then fed into chamber (c). The ratio of the two streams (I:II) is pref. 0.1-0.4:1. In one pref. plant, the molten salt electrolyte leaving chamber (b) is mixed with molten electrolyte leaving the last electrolysis cell in the inlet channel for chamber (c). The yield of Mg per unit of electrical energy is increased; and the purity of the electrolyte fed into the electrolysis cells is raised.</description><subject>APPARATUS THEREFOR</subject><subject>CHEMISTRY</subject><subject>ELECTROLYTIC OR ELECTROPHORETIC PROCESSES</subject><subject>METALLURGY</subject><subject>PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY ORREFINING OF METALS</subject><fulltext>true</fulltext><rsrctype>patent</rsrctype><creationdate>1981</creationdate><recordtype>patent</recordtype><sourceid>EVB</sourceid><recordid>eNqNjDEKwkAQRdNYiHqH6dIouAqi5bCZmIHszrKZ2IYgq41oIN4fI3gAq_94PP48uztSKQQCRahzUSXPjrwKsAcrXtm3AgWDw7OnhmVNEKlG5YsAhoCRrK14Yijrlr9P2DTolSYTuM3BoqNIy2x26x9jWv12kUFJaqtNGl5dGof-mp7p3bEejTkdzA63-z-SD02ZNHY</recordid><startdate>19810209</startdate><enddate>19810209</enddate><creator>VLADIMIR NIKOLAEVICH DEVYATKIN</creator><creator>ILIAS AMALBEKOVICH CHALABAEV</creator><creator>ARNOLD VASILIEVICH KOLOMIITSEV</creator><creator>IGOR VSEVOLODOVICH ZABELIN</creator><creator>MURAT KAZMUKHAMEDOVICH BAIBEKOV</creator><creator>VIKTOR GRIGORIEVICH SOROKOUS</creator><creator>CHAKEN KUDAIBERGENOVICH MEDEUOV</creator><creator>EFIM ALEXANDROVICH KITAIGORODSKY</creator><creator>NIKOLAI MIKHAILOVICH ZUEV</creator><creator>JURY MIKHAILOVICH RYABUKHIN</creator><scope>EVB</scope></search><sort><creationdate>19810209</creationdate><title>METODO PER L'OTTENIMENTO IN CONTINUO DI MAGNESIO,E RELATIVO APPARECCHIO A FLUIDO PASSANTE A PIU' CAMERE</title><author>VLADIMIR NIKOLAEVICH DEVYATKIN ; ILIAS AMALBEKOVICH CHALABAEV ; ARNOLD VASILIEVICH KOLOMIITSEV ; IGOR VSEVOLODOVICH ZABELIN ; MURAT KAZMUKHAMEDOVICH BAIBEKOV ; VIKTOR GRIGORIEVICH SOROKOUS ; CHAKEN KUDAIBERGENOVICH MEDEUOV ; EFIM ALEXANDROVICH KITAIGORODSKY ; NIKOLAI MIKHAILOVICH ZUEV ; JURY MIKHAILOVICH RYABUKHIN</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-epo_espacenet_IT8119612A03</frbrgroupid><rsrctype>patents</rsrctype><prefilter>patents</prefilter><language>ita</language><creationdate>1981</creationdate><topic>APPARATUS THEREFOR</topic><topic>CHEMISTRY</topic><topic>ELECTROLYTIC OR ELECTROPHORETIC PROCESSES</topic><topic>METALLURGY</topic><topic>PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY ORREFINING OF METALS</topic><toplevel>online_resources</toplevel><creatorcontrib>VLADIMIR NIKOLAEVICH DEVYATKIN</creatorcontrib><creatorcontrib>ILIAS AMALBEKOVICH CHALABAEV</creatorcontrib><creatorcontrib>ARNOLD VASILIEVICH KOLOMIITSEV</creatorcontrib><creatorcontrib>IGOR VSEVOLODOVICH ZABELIN</creatorcontrib><creatorcontrib>MURAT KAZMUKHAMEDOVICH BAIBEKOV</creatorcontrib><creatorcontrib>VIKTOR GRIGORIEVICH SOROKOUS</creatorcontrib><creatorcontrib>CHAKEN KUDAIBERGENOVICH MEDEUOV</creatorcontrib><creatorcontrib>EFIM ALEXANDROVICH KITAIGORODSKY</creatorcontrib><creatorcontrib>NIKOLAI MIKHAILOVICH ZUEV</creatorcontrib><creatorcontrib>JURY MIKHAILOVICH RYABUKHIN</creatorcontrib><collection>esp@cenet</collection></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext_linktorsrc</fulltext></delivery><addata><au>VLADIMIR NIKOLAEVICH DEVYATKIN</au><au>ILIAS AMALBEKOVICH CHALABAEV</au><au>ARNOLD VASILIEVICH KOLOMIITSEV</au><au>IGOR VSEVOLODOVICH ZABELIN</au><au>MURAT KAZMUKHAMEDOVICH BAIBEKOV</au><au>VIKTOR GRIGORIEVICH SOROKOUS</au><au>CHAKEN KUDAIBERGENOVICH MEDEUOV</au><au>EFIM ALEXANDROVICH KITAIGORODSKY</au><au>NIKOLAI MIKHAILOVICH ZUEV</au><au>JURY MIKHAILOVICH RYABUKHIN</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>METODO PER L'OTTENIMENTO IN CONTINUO DI MAGNESIO,E RELATIVO APPARECCHIO A FLUIDO PASSANTE A PIU' CAMERE</title><date>1981-02-09</date><risdate>1981</risdate><abstract>The process and plant include a chamber (a) in which fresh MgCl2 is added to an electrolyte; an electrolyte purificn. chamber (b); a chamber (c) for sepg. Mg from the electrolyte; and a chamber (d) which divides the electrolyte into two streams (I,II). One stream (I) is returned to chamber (a) for enrichment with MgCl2; whereas the other (II) is fed through a row of electrolysis cells (e), and is then fed into chamber (c). The ratio of the two streams (I:II) is pref. 0.1-0.4:1. In one pref. plant, the molten salt electrolyte leaving chamber (b) is mixed with molten electrolyte leaving the last electrolysis cell in the inlet channel for chamber (c). The yield of Mg per unit of electrical energy is increased; and the purity of the electrolyte fed into the electrolysis cells is raised.</abstract><edition>3</edition><oa>free_for_read</oa></addata></record> |
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subjects | APPARATUS THEREFOR CHEMISTRY ELECTROLYTIC OR ELECTROPHORETIC PROCESSES METALLURGY PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY ORREFINING OF METALS |
title | METODO PER L'OTTENIMENTO IN CONTINUO DI MAGNESIO,E RELATIVO APPARECCHIO A FLUIDO PASSANTE A PIU' CAMERE |
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