ES8307916A1 - Procedimiento para separar iones manganeso y cloro de una solucion acuosa acida de sulfatos. - Google Patents
Procedimiento para separar iones manganeso y cloro de una solucion acuosa acida de sulfatos.Info
- Publication number
- ES8307916A1 ES8307916A1 ES508321A ES508321A ES8307916A1 ES 8307916 A1 ES8307916 A1 ES 8307916A1 ES 508321 A ES508321 A ES 508321A ES 508321 A ES508321 A ES 508321A ES 8307916 A1 ES8307916 A1 ES 8307916A1
- Authority
- ES
- Spain
- Prior art keywords
- manganese
- zinc
- chloride ions
- treatment
- aqueous acidic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/30—Electrolytic production, recovery or refining of metals by electrolysis of melts of manganese
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/16—Electrolytic production, recovery or refining of metals by electrolysis of solutions of zinc, cadmium or mercury
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B19/00—Obtaining zinc or zinc oxide
- C22B19/20—Obtaining zinc otherwise than by distilling
- C22B19/26—Refining solutions containing zinc values, e.g. obtained by leaching zinc ores
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Electrolytic Production Of Metals (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Saccharide Compounds (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
PROCEDIMIENTO PARA SEPARAR IONES MANGANESO Y CLORO DE UNA SOLUCION ACUOSA ACIDA DE SULFATOS. CONSTA DE LAS SIGUIENTES ETAPAS: 1 ) AJUSTAR LA ACIDEZ LIBRE DE LA SOLUCION A POR LO MENOS 0,1 MOLAR. 2 ) TRATAR LA SOLUCION CON OZONO PARA OXIDAR LOS IONES MANGANESO A DIOXIDO DE MANGANESO. 3 ) CONTINUAR EL TRATAMIENTO CON OZONO UNA VEZ QUE LA CONCENTRACION DE MANGANESO HA DESCENDIDO, PARA OXIDAR IONES CLORO. 4 ) SEPARAR EL DIOXIDO DE MANGANESO DE LA SOLUCION. ANTES DEL TRATAMIENTO CON OZONO, LA SOLUCION CONTIENE DE 100 A 1.000 MG/L APROXIMADAMENTE DE IONES CLORO MIENTRAS QUE DESPUES LA SOLUCION CONTIENE MENOS DE 50 MG/L DE IONES CLORO. LA TEMPERATURA DE LA SOLUCION DURANTE EL TRATAMIENTO CON OZONO ES DE 20 A 60 C APROXIMADAMENTE.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA000378802A CA1166021A (en) | 1981-06-02 | 1981-06-02 | Removal of manganese and chlorine ions from aqueous acidic zinc sulphate solutions |
Publications (2)
Publication Number | Publication Date |
---|---|
ES508321A0 ES508321A0 (es) | 1983-08-16 |
ES8307916A1 true ES8307916A1 (es) | 1983-08-16 |
Family
ID=4120115
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ES508321A Expired ES8307916A1 (es) | 1981-06-02 | 1981-12-23 | Procedimiento para separar iones manganeso y cloro de una solucion acuosa acida de sulfatos. |
Country Status (11)
Country | Link |
---|---|
EP (1) | EP0066024B1 (es) |
JP (1) | JPS57200220A (es) |
KR (1) | KR830007886A (es) |
AU (1) | AU543061B2 (es) |
CA (1) | CA1166021A (es) |
DE (1) | DE3175604D1 (es) |
ES (1) | ES8307916A1 (es) |
FI (1) | FI69125C (es) |
IN (1) | IN157499B (es) |
NO (1) | NO814263L (es) |
ZA (1) | ZA818534B (es) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19640869B4 (de) * | 1996-10-04 | 2010-08-12 | Ruhr-Zink Gmbh | Verfahren zur Gewinnung von Wertmetallen, insbesondere Zink, aus Chlor oder Fluor enthaltenden Rohstoffen |
ES2174190T3 (es) * | 1997-06-20 | 2002-11-01 | Sulfacid S A I F C | Produccion electrolitica de zinc metalico puro a partir de soluciones de zinc contaminadas con maganeso precedida de una desmanganizacion electrolitica en estado frio. |
CN100393897C (zh) * | 2006-09-22 | 2008-06-11 | 云南奥斯迪实业有限公司 | 氢氧化银用于锌电解溶液中脱除氯的工艺 |
CN102828027B (zh) * | 2012-09-18 | 2014-03-19 | 株洲冶炼集团股份有限公司 | 一种铟萃余液中脱除氯的方法 |
CN103668324B (zh) * | 2013-12-06 | 2016-06-29 | 云南祥云飞龙再生科技股份有限公司 | 一种硫酸锌电解废液除氯的工艺 |
CN103952553A (zh) * | 2014-05-13 | 2014-07-30 | 中南大学 | 一种从湿法炼锌溶液脱除氯离子的方法 |
CN114703379B (zh) * | 2022-02-21 | 2023-09-22 | 云锡文山锌铟冶炼有限公司 | 湿法炼锌中性浸出液深度净化的方法 |
CN114772631A (zh) * | 2022-04-20 | 2022-07-22 | 柳州华锡有色设计研究院有限责任公司 | 一种利用臭氧深度脱除ito粉浆中残氯的方法 |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA971368A (en) * | 1972-11-20 | 1975-07-22 | Paul Kawulka | Recovery of zinc from zinc sulphides by direct pressure leaching |
CA1141172A (en) * | 1978-12-20 | 1983-02-15 | Gerald L. Bolton | Removal of manganese ions from zinc and manganese containing solutions |
US4263109A (en) * | 1980-03-31 | 1981-04-21 | Cominco Ltd. | Precipitation of chloride from zinc sulphate solution |
-
1981
- 1981-06-02 CA CA000378802A patent/CA1166021A/en not_active Expired
- 1981-12-04 FI FI813895A patent/FI69125C/fi not_active IP Right Cessation
- 1981-12-07 IN IN769/DEL/81A patent/IN157499B/en unknown
- 1981-12-09 ZA ZA818534A patent/ZA818534B/xx unknown
- 1981-12-11 JP JP56198762A patent/JPS57200220A/ja active Granted
- 1981-12-14 NO NO814263A patent/NO814263L/no unknown
- 1981-12-15 AU AU78532/81A patent/AU543061B2/en not_active Ceased
- 1981-12-17 DE DE8181305929T patent/DE3175604D1/de not_active Expired
- 1981-12-17 EP EP81305929A patent/EP0066024B1/en not_active Expired
- 1981-12-18 KR KR1019810004994A patent/KR830007886A/ko unknown
- 1981-12-23 ES ES508321A patent/ES8307916A1/es not_active Expired
Also Published As
Publication number | Publication date |
---|---|
CA1166021A (en) | 1984-04-24 |
NO814263L (no) | 1982-12-03 |
FI69125B (fi) | 1985-08-30 |
ZA818534B (en) | 1982-12-29 |
ES508321A0 (es) | 1983-08-16 |
EP0066024B1 (en) | 1986-11-12 |
IN157499B (es) | 1986-04-12 |
KR830007886A (ko) | 1983-11-07 |
EP0066024A1 (en) | 1982-12-08 |
DE3175604D1 (en) | 1987-01-02 |
AU543061B2 (en) | 1985-03-28 |
JPH0255374B2 (es) | 1990-11-27 |
FI69125C (fi) | 1985-12-10 |
FI813895A0 (fi) | 1981-12-04 |
JPS57200220A (en) | 1982-12-08 |
AU7853281A (en) | 1982-12-09 |
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