DE370194C - Electrolytic tin bath for the representation of sponge-free tin crystals - Google Patents

Electrolytic tin bath for the representation of sponge-free tin crystals

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Publication number
DE370194C
DE370194C DER56580D DER0056580D DE370194C DE 370194 C DE370194 C DE 370194C DE R56580 D DER56580 D DE R56580D DE R0056580 D DER0056580 D DE R0056580D DE 370194 C DE370194 C DE 370194C
Authority
DE
Germany
Prior art keywords
tin
sponge
sulfuric acid
representation
crystals
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
Application number
DER56580D
Other languages
German (de)
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
THERESE ROCKSCH GEB LASCHET
Original Assignee
THERESE ROCKSCH GEB LASCHET
Publication date
Priority to DER56580D priority Critical patent/DE370194C/en
Application granted granted Critical
Publication of DE370194C publication Critical patent/DE370194C/en
Expired legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C5/00Electrolytic production, recovery or refining of metal powders or porous metal masses
    • C25C5/02Electrolytic production, recovery or refining of metal powders or porous metal masses from solutions

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  • 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 Metals (AREA)
  • Catalysts (AREA)

Description

Elektrolytisches Zinnbad zur Darstellung schwammfreier Zinnkristalle. Bei der galvanischen Entzi,nnuin,g zinnhaltiger Abfälle sowie bei Raffinatnonsprozessen wird das Zinn größtenteils als Sch@wamm@ gewonnen, der, aus höchst fein verteiltem Zinn bestehend, große Neigung zur Oxydation hat, beim :Einschmelizen ,durch Verbrennung über 5o Prozent oxydischen Rückstand iergiibt, der einer erneuten Aufarbeitung .bedarf. Lötmittel in Salben- und: Stangenform, zu deren Darstefung ,man. @meist gal"vanisah nfiedergesehlagernes Zinn verwendet, verbrennen zum Teil bei der Anwe@ndumg, wodurch die Wirkung beeinträchtigt wird'. Dieser Übelstand wird- durch ,das ,nachstehend beschräebene Verfa,hren vermieden, dienn es gelingt damit, große Kristalle zu erzeugen, die -sich fasst verlustfrei schmelzen lassen, die man aber, wenn sie zu Lötmitteln verwendet werden sollen, leicht zerkleinern kann. Der Elektrolyt ist ferner vorteilhaft zur Trennung des Quecksilbers von, Zinn (Spii-egelamaligam) zu: gebrauahen. Es ,biliden sich die ZnnnkrIstalle, während metallisches Ouecksiilber zurückbleibt. Zur Raenation jes Zinns verwendet, findet man beim E lektrolysieren ,das Blei ,des stark bleihaltigen Materials nur in !Spuren ir_ den Kristallen vor. Es hat sich gezeigt, daß diese schwammfrefen, großen. Zinnkristalle entflohen, wenn der Elektrolyt aus einer ziemlich konzentrierten 7inrnsavzlösuing besteht, welchem man: Schwefelsäure oder schwefelsaure Sa ze (sauer oder neutral) zusetzt, und zwar erwies sich amvorteiilhaftesten I. eine wäßrige Lösung, die im i- ooo Teilen 1 25 gkrist. Zi@nnchlorür und 25 g engl.Schrwefelsäure oder II. .eine wäßnige Zin:rnsalizlösung, die in i ooo Teilen Zoo g krist. Zinnchlorür und' 65 g Alu ,nvi-niumsu @fat oder ein anderes schwefelsaures Salz enthfelt.Electrolytic tin bath for the representation of sponge-free tin crystals. In the galvanic ignition of waste containing tin, as well as in raffinate processes, the tin is obtained for the most part as Sch @ wamm @, which, consisting of extremely finely divided tin, has a great tendency to oxidize, when: melting down, by incineration over 50 percent oxidic residue iergiibt, which needs a renewed work-up. Solder in the form of an ointment and: rod, for their presentation, man. @ mostly gal "vanisah nfiedergesehlstornes tin used, burns in part during use, whereby the effect is impaired. which can be melted without loss, but which can easily be crushed if they are to be used for soldering agents. The electrolyte is also advantageous for separating the mercury from the tin (Spii-egelamaligam) to: used. They form Tin crystals, while metallic silver remains. Used to refine this tin, one finds only traces of lead in the crystals during electrolysis The electrolyte consists of a fairly concentrated solution to which: sulfuric acid or sulfuric acid salts (acidic or neutral) are added, and Although I. proved to be the most advantageous an aqueous solution containing in 100 parts 1 25 g; Zinc chloride and 25 g of English sulfuric acid or II. An aqueous solution of tin: saline which, in 10000 parts, is crystalline. Tin chloride and 65 g aluminum, nvi-niumsu @fat or another sulfuric acid salt.

Man elektrolysiert mit 2 Abis 4 Volt mit Kathoden aus Eisenblech usw., während die Anoden aus Zinn, Di.nnmetallhaltiggen Abfällen wie We'ißblech usw. bestehen können. Blei spiele: Auf i >i des Bades 25o g Zinnlauge mit 50 Prozent S*Cl'z+2aq, 25 g engl. Schwefelsäure, 725 g Wasser.Electrolysis is carried out with 2 to 4 volts with cathodes made of sheet iron, etc., while the anodes may consist of tin, waste containing non-ferrous metals such as white sheet, etc. Lead games: On i> i of the bath 25o g tin lye with 50 percent S * Cl'z + 2aq, 25 g engl. Sulfuric acid, 725 g water.

400 9 C,hilorziun:laug e mit 50 Prozent Sn Cl 2 -f- 2 aq, 65 g Aluminiumsulfat, 535 9 Wasser.400 9 C, hilorziun: lye with 50 percent Sn Cl 2 -f- 2 aq, 65 g aluminum sulfate, 535 9 water.

Claims (1)

PATENTANSPRUCH: Edektrolyti:sches .Zinnbad zur Darstellung schwammfreier Zi@nnkni,stall,e, dadurch ,gakennzeichrnet, daß rain einer Zinn-@satzlösung einen Zusatz von Schwefelsäure oder schwefelsauren Salzen (sauer oder neutral) macht, dergestalt"daß in ioo Teilen I. i2,5 Teile Zinnsalz Sn Cl 2 -f- 2 aq, 2,2 - engl. Schwefelsäure, 85 - Wasser oder II. 2a Teile Zinnsalz Sn. Cl 2 + 2 aq, 6,5 - Aluminivumsulfat oder ein anderes schwefelsaures Salz, 74,5 - Wasser enthalten sind. PATENT CLAIM: Edektrolyti: sches .Zinnbad for the production of sponge-free Zi @ nnkni, stall, e, characterized by the fact that a tin substitute solution makes an addition of sulfuric acid or sulfuric acid salts (acidic or neutral), in such a way "that in 100 parts I 1.5 parts tin salt Sn Cl 2 -f- 2 aq, 2.2 - English sulfuric acid, 85 - water or II.2a parts tin salt Sn.Cl 2 + 2 aq, 6.5 - aluminum sulfate or another sulfuric acid salt , 74.5 -water are included.
DER56580D Electrolytic tin bath for the representation of sponge-free tin crystals Expired DE370194C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DER56580D DE370194C (en) Electrolytic tin bath for the representation of sponge-free tin crystals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DER56580D DE370194C (en) Electrolytic tin bath for the representation of sponge-free tin crystals

Publications (1)

Publication Number Publication Date
DE370194C true DE370194C (en) 1923-02-28

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Family Applications (1)

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DER56580D Expired DE370194C (en) Electrolytic tin bath for the representation of sponge-free tin crystals

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DE (1) DE370194C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11291645B2 (en) 2002-10-23 2022-04-05 Vifor (International) Ag Aqueous iron carbohydrate complexes, their production and medicaments containing them
US11344568B2 (en) 2006-01-06 2022-05-31 American Regent, Inc. Methods and compositions for administration of iron

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11291645B2 (en) 2002-10-23 2022-04-05 Vifor (International) Ag Aqueous iron carbohydrate complexes, their production and medicaments containing them
US11590097B2 (en) 2002-10-23 2023-02-28 Vifor (International) Ag Aqueous iron carbohydrate complexes, their production and medicaments containing them
US11344568B2 (en) 2006-01-06 2022-05-31 American Regent, Inc. Methods and compositions for administration of iron
US11364260B2 (en) 2006-01-06 2022-06-21 American Regent, Inc. Methods and compositions for administration of iron
US11406656B2 (en) 2006-01-06 2022-08-09 American Regent, Inc. Methods and compositions for administration of iron
US11433091B2 (en) 2006-01-06 2022-09-06 American Regent, Inc. Methods and compositions for administration of iron
US11478502B2 (en) 2006-01-06 2022-10-25 American Regent, Inc. Methods and compositions for administration of iron

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