SU536256A1 - The method of separation of metals by potentiostatic electrolysis - Google Patents
The method of separation of metals by potentiostatic electrolysisInfo
- Publication number
- SU536256A1 SU536256A1 SU2156397A SU2156397A SU536256A1 SU 536256 A1 SU536256 A1 SU 536256A1 SU 2156397 A SU2156397 A SU 2156397A SU 2156397 A SU2156397 A SU 2156397A SU 536256 A1 SU536256 A1 SU 536256A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- metals
- separation
- potentiostatic electrolysis
- electrolysis
- potentiostatic
- Prior art date
Links
Landscapes
- Electrolytic Production Of Metals (AREA)
Description
ни ДЭС. Дл высокотемпературных чеек специальной конструкции значение Ком может быть сведено к пренебрежимому минимуму . Тогда диапазон перекрывани будет определ тьс только величиной U . Поскольку в солевых расплавах пол ризаци имеет только концентрационный характер , то справедливо выражениеnor DES. For high-temperature cells of a special design, the value of Kom can be reduced to a negligible minimum. Then the overlap range will be determined only by the value of U. Since in salt melts polarization has only a concentration character, the expression
vif--evif - e
) (О) (ABOUT
При L|(;,0,99 L искомый диапазон перекрывани дУ может быть определен по отношению.At L | (;, 0.99 L, the desired range of overlap of the remote control can be determined by the ratio.
1one
AU 5/)0. - (2)AU 5 /) 0. - (2)
Дл практически используемого при электролизе расплавленных солевых средств интервала температур от 623 до 1173°К и возможной валентности выдел емых металлов Z 1-4 диапазон перекрывани составит 0,05-0,50В. При величине заданного потенциала, перекрывающей потенциал вьщелени конкурирующего компонента на 0,05-0,50В, требуема избирательность может быть обеспечена лишь при об зательном прекращении электролиза в момент стабилизации тока. При этом с ростом ли увеличиваетс и ..Q Пример . Провод т потенциостатическое растворение церий-алюминиевых сплавов ( SA 1 см ) в электролите КС -NaCFor the range of temperatures from 623 to 1173 ° K and the possible valence of released metals Z 1-4, which is practically used in the electrolysis of molten salt means, the overlap range will be 0.05-0.50 V. When the value of a given potential, which overlaps the potential of the competing component at 0.05-0.50 V, the required selectivity can be ensured only with a mandatory cessation of electrolysis at the moment of current stabilization. At the same time, as it grows, it increases and ..Q Example. Potentiostatic dissolution of cerium-aluminum alloys (SA 1 cm) in electrolyte KS -NaC
при 700-С. Электродом сравнени служит хлорный полуэлемент. Данные приведены в таблице.at 700 ° C. The reference electrode is chlorine half cell. The data are given in the table.
Избирательность процесса не тсудшаетс , если работать при заданном потен-The selectivity of the process does not deteriorate if working at a given potential
циале (-2,00 В), перекрывающем потенциал начала вьщелени алюмини (-2,15В), на 0,15 В, с прекращением электролиза при У стаб. - 0,013 А, но могут быть достигнуты больша скорость и меньша The dial (-2.00 V), which covers the potential for the onset of aluminum (-2.15 V), at 0.15 V, with the termination of the electrolysis at Y stub. - 0.013 A, but greater speed and less can be achieved
длительность процесса. Расчет по уравнению (2) дает дУ 0,13 В. По-видимому расхождение в 0,02 В между эксперименлом и расчетом обусловлено омическими потер ми и Qjthe duration of the process. The calculation by equation (2) gives a DU of 0.13 V. Apparently, a difference of 0.02 V between the experiment and the calculation is due to ohmic losses and Qj
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU2156397A SU536256A1 (en) | 1975-07-19 | 1975-07-19 | The method of separation of metals by potentiostatic electrolysis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU2156397A SU536256A1 (en) | 1975-07-19 | 1975-07-19 | The method of separation of metals by potentiostatic electrolysis |
Publications (1)
Publication Number | Publication Date |
---|---|
SU536256A1 true SU536256A1 (en) | 1976-11-25 |
Family
ID=20626660
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU2156397A SU536256A1 (en) | 1975-07-19 | 1975-07-19 | The method of separation of metals by potentiostatic electrolysis |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU536256A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2578279C2 (en) * | 2013-07-05 | 2016-03-27 | Кабусики Кайся Тосиба | Method of separation and extraction of metals and system for separation and extraction of metals |
-
1975
- 1975-07-19 SU SU2156397A patent/SU536256A1/en active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2578279C2 (en) * | 2013-07-05 | 2016-03-27 | Кабусики Кайся Тосиба | Method of separation and extraction of metals and system for separation and extraction of metals |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AT355816B (en) | ELECTROCHEMICAL METHOD FOR THE ELECTROLYSIS OF METALS OR METAL-CONTAINING SOLUTIONS OR FOR THE ELECTROSYNTHESIS OF COMPOUNDS, AND ELECTROCHEMICAL CELL FOR IMPLEMENTING THE METHOD | |
GB1528475A (en) | Process for extracting metal ions from a solution of a salt of the metal | |
BE837758A (en) | PRODUCTION OF CARBONATES FROM ALKALINE METALS IN AN ELECTROLYTIC MEMBRANE CELL | |
SU536256A1 (en) | The method of separation of metals by potentiostatic electrolysis | |
GB1533542A (en) | Separation and purification of platinum and palladium | |
GB1325981A (en) | Production of copper silver or mercury | |
GB575001A (en) | A method of purifying zinc electrolytes | |
FR2276400A1 (en) | METAL ELECTRODE FOR ELECTROLYSIS CELL OF ALKALINE HALOGENIDE SOLUTIONS | |
SE7509050L (en) | ELECTROLYSIS EXTRACTION OF METALS | |
SE7602227L (en) | ELECTROLYTICAL PROCEDURE FOR EXTRACTION OF METALS IN POWDER | |
GB1507018A (en) | Electrolytic trapping of iodine from process gas streams | |
JPS5319171A (en) | Separating and recovering method of good efficiency for acid and metal from solution containing acid and metal salt | |
IS2190A7 (en) | Process for the production of metals by electrolysis of molten metal salts, chlorine salts, metals and electrolytes to carry out the process. | |
SU560927A1 (en) | Method of stabilizing amino chloride electrolyte | |
Ferrett et al. | Studies in polarography. Part 1.—The rotating platinum electrode | |
SU1083096A1 (en) | Electrolyte for colored electrochemical etching of titanium alloys | |
GB1049709A (en) | A process for isolating metals from solutions containing them, and novel pyridine n-oxides used for the purpose | |
SU773113A1 (en) | Method of electroleaching of zinc-containing materials | |
JPS52128804A (en) | Electrolytic recovery of metal | |
SU135643A1 (en) | Indie refining method of thallium | |
Denham et al. | 331. The ternary system mercurous oxide–nitrogen pentoxide–water | |
JPS52143973A (en) | Production of electrolytic solution | |
Sakai | The Ultraviolet Absorption Spectra of the Molten and Solidified Mixed Salt Systems NaNO 2-NaNO 3, NaCl-CdCl 2 | |
KR830010209A (en) | How to recover uranium | |
GB927285A (en) | A new or improved process for the manufacture of microporous metallic membranes |