DE720663C - Production of zinc powder from zinc salt solutions - Google Patents
Production of zinc powder from zinc salt solutionsInfo
- Publication number
- DE720663C DE720663C DES137041D DES0137041D DE720663C DE 720663 C DE720663 C DE 720663C DE S137041 D DES137041 D DE S137041D DE S0137041 D DES0137041 D DE S0137041D DE 720663 C DE720663 C DE 720663C
- Authority
- DE
- Germany
- Prior art keywords
- zinc
- value
- powder
- zinc powder
- solution
- 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
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title claims description 15
- 150000003751 zinc Chemical class 0.000 title claims description 7
- 239000012266 salt solution Substances 0.000 title claims description 5
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- 239000000243 solution Substances 0.000 claims description 15
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 14
- 235000005074 zinc chloride Nutrition 0.000 claims description 7
- 239000011592 zinc chloride Substances 0.000 claims description 7
- 235000002639 sodium chloride Nutrition 0.000 claims description 6
- 150000003839 salts Chemical class 0.000 claims description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 3
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 claims description 2
- 230000007062 hydrolysis Effects 0.000 claims description 2
- 238000006460 hydrolysis reaction Methods 0.000 claims description 2
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 claims 3
- 150000001450 anions Chemical class 0.000 claims 1
- 238000005868 electrolysis reaction Methods 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 229910052725 zinc Inorganic materials 0.000 description 3
- 239000011701 zinc Substances 0.000 description 3
- 230000002349 favourable effect Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- -1 B. The alkalis Chemical class 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000337 buffer salt Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- OVSQVDMCBVZWGM-QSOFNFLRSA-N quercetin 3-O-beta-D-glucopyranoside Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=C(C=2C=C(O)C(O)=CC=2)OC2=CC(O)=CC(O)=C2C1=O OVSQVDMCBVZWGM-QSOFNFLRSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C5/00—Electrolytic production, recovery or refining of metal powders or porous metal masses
- C25C5/02—Electrolytic production, recovery or refining of metal powders or porous metal masses from solutions
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrolytic Production Of Metals (AREA)
Description
Herstellung von Zinkpulver aus Zinksalzlösungen Die Darstellung von Zinkpulver .auf elektrolytischem Wege aus nichtalkalischen Zinksalzlösungen ist an die Anwendung hoher Stromdichten (etwa bis 5oooA,'m°-) und nicht zu hoher 1Zetallkonzentration im Elektrolyten gebunden, wobei rdie Temperatur der Elektrolyselösung noch zusätzlich geändert werden kann.- Hierbei erhält man aber nur grobkörnige bis schuppenartige Produkte. Feinere Pulver werden fast ,ausschließlich aus alkalischer Zinkatlösung erzeugt. -Bekannt ist auch, dem Elektrolyten Stoffe :organischer Art oder auch Fremdmetalle zuzusetzen.Production of zinc powder from zinc salt solutions The representation of Zinc powder. Is electrolytically made from non-alkaline zinc salt solutions to the use of high current densities (up to about 5oooA, 'm ° -) and not too high a metal concentration bound in the electrolyte, with r the temperature of the electrolysis solution additionally can be changed.- Here you only get coarse-grained to flaky Products. Finer powders are made almost exclusively from an alkaline zincate solution generated. Also known is the electrolyte substances: organic or foreign metals to add.
Es wurde nun gefunden, daß man auch aus schwach sauren Zinksalzlösungen, die noch fremde Salze, z. B. .der Alkalien, enthalten, Zink in feinpul-°riger Form erhalten kann. wenn man bei der Elektrolyse den Säuregrad (pH-Wert) der Lösung und die Stromdichte in bestimmten engen Grenzen hält. Hierbei kann man durch Anwendung verschiedener Konzentration des Elektrolyten wie auch der Temperatur die gewünschten pulverförmigen Produkte erhalten.It has now been found that weakly acidic zinc salt solutions, the still foreign salts, e.g. B. The alkalis, contain zinc in fine powder form can get. if you check the acidity (pH value) of the solution during electrolysis and keeps the current density within certain narrow limits. This can be done by applying different concentration of the electrolyte as well as the temperature the desired powdered products obtained.
Von besonderer Bedeutung für diese Art der Zinkstaubgewinnung ist der pH-Wert der Lösung. Aus einer sauren Lösung, z. B. PH 3,o, läßt sich das Zink nur als festes Metall ,an der Kathode .niederschlagen. Selbst bei PH-Werten von .1 bis 4,5 werden bekanntlich noch zusammenhä ngende Niederschläge und kein Zinkpulver erhalten. Bei einem PH-Wert von z. B. über 6,o erhält- man hingegen bei normaler Temperatur aus einer Zinkchloridlösun,g einen stark durch Hydrosyd verunreinigten Metallschwamm. Vollkommen einwandfreie Zinkpulverniederschläge wurden nur im Bereich von über PH 45 bis 5,8, vorzugsweise PH 5,o bis 5,5, erhalten. Der p11-Wert darf nicht höher sein als der Wert, bei dem die Hydrolyse des betreffenden Zinksalzes (z. B. bei Zinkchlorid PH = 5,8) einsetzt. Das Zinkpulver wird uin so feiner, je geringer der Säuregrad des Elektrolyten ist. Die kathodische Stromdichte wird auf einem Wert von goo bis iooo A,lm° gehalten.Of particular importance for this type of zinc dust extraction is the pH of the solution. From an acidic solution, e.g. B. PH 3, o, the zinc only as solid metal, deposited on the cathode. Even with pH values of .1 to 4.5 are known to be coherent precipitates and no zinc powder obtain. At a pH of z. B. over 6, o is obtained with normal Temperature from a zinc chloride solution, a heavily contaminated by hydroside Metal sponge. Flawless zinc powder precipitates were made obtained only in the range from above PH 45 to 5.8, preferably PH 5, o to 5.5. Of the p11 value must not be higher than the value at which the hydrolysis of the relevant Zinc salt (e.g. with zinc chloride PH = 5.8) is used. The zinc powder will be like this finer, the lower the acidity of the electrolyte. The cathodic current density is held at a value from goo to iooo A, lm °.
Es ist' ferner gefunden worden, daß man unter Beachtung des günstigsten pii-Bereiches zur Erzielung einer wirtschaftlichen Herstellung (günstigen Energieausbeute) statt einer Herabsetzung des Zinkgehaltes der Lösung besser der Lösung durch Zusatz von Puffersalzen den gewünschten pH-Wert und eine hohe Leitfähigkeit erteilt. Durch Anwendung gleichioniger Salze setzt mau dabei die wirksame Zinkionenkonzentration auf ein gewünschtes Maß herab. Mau wird also bei der Elektrolyse d'mer Zin.kchloridlösung das billige Kochsalz zusetzen. Anwendung höherer Temperatur bei der Elektrolyse ist von Vorteil. Auch hier läßt sich die Erzielung von gewünschter Kornfeinheit durch Einregeln des p1.1-Wertes bei nicht allzu hohen Stromdichten durchführen. Ausführungsbeispiele i. Aus einer Zinkchloridlösung wurde bei einem pH-Wert von 5,5 und einer kathodischen Stromdichte von ioooA/m= ein Zinkpulver erhalten, das 5% Korn 0,3 bis o,6mm, 330/0 von 0,15 bis o,3 mm, 3 i oio von 0,075 bis 0,15n-im und 3 i % unter o,o75 mm enthielt.It has also been found that, taking into account the most favorable pii range to achieve economical production (favorable energy yield), instead of reducing the zinc content of the solution, it is better to give the solution the desired pH value and high conductivity by adding buffer salts. By using salts of the same ion, the effective zinc ion concentration is reduced to a desired level. Mau will therefore add the cheap table salt to the electrolysis of a zinc chloride solution. Use of higher temperatures for electrolysis is an advantage. Here, too, the desired grain fineness can be achieved by adjusting the p1.1 value with the current densities not being too high. Embodiments i. A zinc powder was obtained from a zinc chloride solution at a pH of 5.5 and a cathodic current density of 100A / m = 5% grain 0.3 to 0.6 mm , 330/0 from 0.15 to 0.3 mm , 3 i oio contained from 0.075 to 0.15 n-im and 3 i% below 0.075 mm.
2. Aus einer Zinkchloridlösung wurde bei einen. pH-Wert von 4,9 und einer kathodischen Stromdichte von 98o A/m°- ein Zinkpulver erhalten, das ii,5% Korn von 0,3 bis o,6mm, 3 i % von o, 15 bis 0,3 mm, 29,5 % von o,075 bis o, 15 mm und 27,2 % unter o,075 mm enthielt. Der Rest war größer als o,6 mm.2. A zinc chloride solution turned into a. obtain a zinc powder, ii, 5% grain from 0.3 to o, 6mm, 3% i o, 1 5 to 0.3 mm - pH-value of 4.9 and a cathodic current density of 98o A / m ° , contained 29.5% of o, o to 075, 1 5 mm and 27.2% of O, 075 mm. The rest was larger than 0.6 mm.
Durch Ändern der Stromdichte kann die Kornfeinheit beeinflußt werden, weil. bei höheren Stromdichten bei gleichem pH-Wert feineres Pulver entsteht.The grain fineness can be influenced by changing the current density, because. at higher current densities at the same pH value, finer powder is produced.
Durch Anwendung von Diaphragmen können bei Verwendung unlöslicher Anoden die anodischen Produkte, z. B. Chlor ,aus Chloridlösung; gewonnen. werden.By using diaphragms, insoluble Anodes the anodic products, e.g. B. chlorine, from chloride solution; won. will.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DES137041D DE720663C (en) | 1939-05-12 | 1939-05-12 | Production of zinc powder from zinc salt solutions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DES137041D DE720663C (en) | 1939-05-12 | 1939-05-12 | Production of zinc powder from zinc salt solutions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE720663C true DE720663C (en) | 1942-05-12 |
Family
ID=7540482
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DES137041D Expired DE720663C (en) | 1939-05-12 | 1939-05-12 | Production of zinc powder from zinc salt solutions |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE720663C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2673178A (en) * | 1950-09-01 | 1954-03-23 | Daniel W Duncan | Electrolysis of zinc chloride |
| US2673179A (en) * | 1950-09-01 | 1954-03-23 | Daniel W Duncan | Process for the recovery of zinc |
| DE1198073B (en) * | 1963-01-05 | 1965-08-05 | Lonza Ag | Process for the electrolytic production of highly dispersed lead or zinc |
-
1939
- 1939-05-12 DE DES137041D patent/DE720663C/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2673178A (en) * | 1950-09-01 | 1954-03-23 | Daniel W Duncan | Electrolysis of zinc chloride |
| US2673179A (en) * | 1950-09-01 | 1954-03-23 | Daniel W Duncan | Process for the recovery of zinc |
| DE1198073B (en) * | 1963-01-05 | 1965-08-05 | Lonza Ag | Process for the electrolytic production of highly dispersed lead or zinc |
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