[go: up one dir, main page]

US792307A - Process of electrodepositing antimony. - Google Patents

Process of electrodepositing antimony. Download PDF

Info

Publication number
US792307A
US792307A US20894404A US1904208944A US792307A US 792307 A US792307 A US 792307A US 20894404 A US20894404 A US 20894404A US 1904208944 A US1904208944 A US 1904208944A US 792307 A US792307 A US 792307A
Authority
US
United States
Prior art keywords
antimony
solution
anode
electrodepositing
cathode
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 - Lifetime
Application number
US20894404A
Inventor
Anson Gardner Betts
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.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US20894404A priority Critical patent/US792307A/en
Application granted granted Critical
Publication of US792307A publication Critical patent/US792307A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/54Electroplating: Baths therefor from solutions of metals not provided for in groups C25D3/04 - C25D3/50

Definitions

  • Figure 1 is a view in vertical cross-sectionin which I show apparatus arranged for the deposition of antimony from a fluorid solution with an insoluble anode.
  • My invention consists, partly, in elec'tro-' depositing antimony fromsolutions contain-.
  • Antimony trifluorid differs from theordinary antimony salts in not being decomposed by water intoinsoluble basic antimony compounds and free acid, so that a depositing solution can be prepared which is only slightly acid. The presence of large quantities of free acids, especially halogen acids, is not desir able.
  • the fluorid solution has the advantage that if an insoluble anode is used oxygen gas is there given ,ofl" and hydrofluoric acid formed,
  • Hydrofluoric acid is a good solvent for antimony oxids and basic compounds, so that the solution after electrolysis with an insoluble anode is in snitable condition for dissolving fresh amounts of basic antimony compounds from which it is desired to prepare metallic antimony.
  • the electrolytic bath contain in addition to antimony trifluorid salts of metals which will not deposit on the cathodes with antimony.
  • the alkali sulfates and fluorids are most suitable.
  • an antimony anode is being used in the electrolysis alllmline chlorids may be used with 'good resu ts.
  • Lead makes the most suitable insoluble anode, which should consist of lead rods to which free access of solution should be prevented by a layer of porous material, preferably by a few layers of cloth surrounding each rod.
  • the antimony has a tendencyto become oxidized to the pentavalent form at the anode, in which form it has a dissolving action on the metal of the cathode, being there reduced If the cloth is absent, enough oxidation of the antimony inthe solution may occur to reduce the actual yield of metal deposited at the cathode to sixty per cent. of what should be theoretically obtained by the amount of electricity passed, while with anodes wrapped in cloth the yield rises to from ninety to ninety-five per cent.
  • the anode area should not be over half of the cathode area, because with the higher anode current density the formation of pentavalentantimony compounds is reduced.
  • the voltage'required, using insoluble anodes, is usually from 2.5 to three volts.
  • sulfate I mean to include sulfuric acid, as it-is a sulfate of hydrogen.
  • Fig. 1 shows in vertical cross-section a tank 1, containing the antimony solution 2, cathodes 3, on which antimony .4 has been deposited, and anodes of lead 5, surroundedby cloth 5.
  • Fig. 2' shows in vertical cross-section a tank 7, containing the anti-. mony solution 8, in. which is suspended an antimony anode 9, partly dissolved byelectrolysis, while a corresponding amount of purified antimony has been deposited on the cathode 10.
  • Jnony whichconsists in electrolyzing a solution containing antimony trifluorid with an insol u- 2.
  • the process of electrodepositing antimony which consists in electrolyzing a solution containingantimony trifl'uorid and a sulfate with a suitable cathode.
  • Jnony whichconsists in electrolyzing a solution containing antimony trifluorid with an insol u- 2.
  • the process of electrodepositing antimony which consists in electrolyzing a solution containingantimony trifl'uorid and a sulfate with a suitable cathode.

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)

Description

' No; 792,307. PATENTED JUNE113, 1905.
A. G. BBT'I'S. PROCESS OF BLEGTRODEPOSITING ANITIMONY.
APLIOATIOH FILED MAY 20, 1904.
IUVE'ITIBR U ITE STATES Patented an... 13, 1905.
PA'IIIENT OFFICE.-
PROGEdS- 0 ELECTRODEIPOSITING uTmoNY.
SPECIFICATION'fwming part of Letters Patent No. 792,307, dated June 13, 1905.
Application filed Kay 20, 1904. Serial No. 208,944.
A To all whom it may concern:
Be it known that I, Anson GARDNER Bn'rrs,
a citizen of the United States, residing at Troy, county of Rensselacr, and State of New York, have invented certain new and useful Im provements in Processes of Electrodepositing Antimony, of which the following is a specification accompanied by drawings.
Figure 1 is a view in vertical cross-sectionin which I show apparatus arranged for the deposition of antimony from a fluorid solution with an insoluble anode. Fig. 2 shows in vertical cross-section apparatus arranged for =tion is desirable.
the deposition of antimony, using an antimony anode.
My invention; consists, partly, in elec'tro-' depositing antimony fromsolutions contain-.
'ing antimony trifluorid, using eithen'antimony anodes or insoluble anodes. .Antimony trifluorid differs from theordinary antimony salts in not being decomposed by water intoinsoluble basic antimony compounds and free acid, so that a depositing solution can be prepared which is only slightly acid. The presence of large quantities of free acids, especially halogen acids, is not desir able.
. The fluorid solution has the advantage that if an insoluble anode is used oxygen gas is there given ,ofl" and hydrofluoric acid formed,
I which remains in solution. Hydrofluoric acid is a good solvent for antimony oxids and basic compounds, so that the solution after electrolysis with an insoluble anode is in snitable condition for dissolving fresh amounts of basic antimony compounds from which it is desired to prepare metallic antimony.
I prefer to have the electrolytic bath contain in addition to antimony trifluorid salts of metals which will not deposit on the cathodes with antimony. The alkali sulfates and fluorids are most suitable. In case an antimony anode is being used in the electrolysis alllmline chlorids may be used with 'good resu ts.
The presence of sulfuric. acid in the solu- A suitable solution contains eight per cent. SbFa, two per cent. NazSO4, and fourIper cent. H2804. A current density of ten amperes per square foot gives a. good again to the trivalent form.
deposit of antimony when the solution is purethat is, free from metals which would deposit with the antimony. By electrolyzing such a solution with an insoluble anode such I a solution can be largely deprived of antimony, oxygen escaping at'the anode and leaving a solution containing hydrofluoric acid.
Lead makes the most suitable insoluble anode, which should consist of lead rods to which free access of solution should be prevented by a layer of porous material, preferably by a few layers of cloth surrounding each rod. The antimony has a tendencyto become oxidized to the pentavalent form at the anode, in which form it has a dissolving action on the metal of the cathode, being there reduced If the cloth is absent, enough oxidation of the antimony inthe solution may occur to reduce the actual yield of metal deposited at the cathode to sixty per cent. of what should be theoretically obtained by the amount of electricity passed, while with anodes wrapped in cloth the yield rises to from ninety to ninety-five per cent.
. The anode area should not be over half of the cathode area, because with the higher anode current density the formation of pentavalentantimony compounds is reduced. The voltage'required, using insoluble anodes, is usually from 2.5 to three volts.
By the term sulfate I mean to include sulfuric acid, as it-is a sulfate of hydrogen.
Having reference the accompanying drawings, Fig. 1 shows in vertical cross-section a tank 1, containing the antimony solution 2, cathodes 3, on which antimony .4 has been deposited, and anodes of lead 5, surroundedby cloth 5.- Fig. 2'shows in vertical cross-section a tank 7, containing the anti-. mony solution 8, in. which is suspended an antimony anode 9, partly dissolved byelectrolysis, while a corresponding amount of purified antimony has been deposited on the cathode 10.
What I claim as new, and by'Letters Patent, is- I 1.,The process of e1ectrodepositing=anti-. mony which consists in electrolyzing-a solution desire to secure containing antimony trifluorid with a suitable cathode.
"Disclaimer in .Let ters- Patent No, 792,307.
solution. containing antimony January/v80, r
Jnony whichconsists in electrolyzing a solution containing antimony trifluorid with an insol u- 2. The process of electrodepositing antimony which consists in electrolyzing a solution containingantimony trifl'uorid and a sulfate with a suitable cathode.
3. The process-of electrodepositing antible anode' and with a suitable cathode.
4. The process of electrodepositing antii'nony which consists in electrolyzing a solution anode and with a suitable cathode 5. The 'process of electrodepositing antimony which consists in electrolyzinga solution containing antimony trifluorid with a lead-\ anode and with a suitable" cathode, and p'reventing free circulation of the entire solution to the anode by means of a layer of porous j material. v
6. The process ofelectrodepositing antimony which consists in electrolyzing a solution containing antimony trifluorid with an insoluble anode having an ele'ctroly-zi'ng-surface con- V siderably smaller than the cathode-surface,
and with a suitable cathode. y
In testimony whereof I have signed my nam to this specification in presence of two subscribing witnesses. N
i AN SON GARDNER BET'IS.
Witnesses: v I
EDWARD FQKERN, WILLIAM VALENTINE.
DISCLAIMER.
792,3( )7.Anaon Gardner Betta; Troy, N PRocEss'oF ELEdTaonnrosm'nIe AN'IIlKONY- Patent dated June-l3, 1905.- Disclaimer filed January 24, 1906, by the patentee.
Enters his disclaimer- To claim- No. 1, which reads as follows, to wit: a
1. The process of electrodepositing antimony which consists in .electroly'zing a --triflnorid with a suitable cathode.-[Ofiim'al Gazette "Disclaimer in .Let ters- Patent No, 792,307.
solution. containing antimony January/v80, r
Jnony whichconsists in electrolyzing a solution containing antimony trifluorid with an insol u- 2. The process of electrodepositing antimony which consists in electrolyzing a solution containingantimony trifl'uorid and a sulfate with a suitable cathode.
3. The process-of electrodepositing antible anode' and with a suitable cathode.
4. The process of electrodepositing antii'nony which consists in electrolyzing a solution anode and with a suitable cathode 5. The 'process of electrodepositing antimony which consists in electrolyzinga solution containing antimony trifluorid with a lead-\ anode and with a suitable" cathode, and p'reventing free circulation of the entire solution to the anode by means of a layer of porous j material. v
6. The process ofelectrodepositing antimony which consists in electrolyzing a solution containing antimony trifluorid with an insoluble anode having an ele'ctroly-zi'ng-surface con- V siderably smaller than the cathode-surface,
and with a suitable cathode. y
In testimony whereof I have signed my nam to this specification in presence of two subscribing witnesses. N
i AN SON GARDNER BET'IS.
Witnesses: v I
EDWARD FQKERN, WILLIAM VALENTINE.
DISCLAIMER.
792,3( )7.Anaon Gardner Betta; Troy, N PRocEss'oF ELEdTaonnrosm'nIe AN'IIlKONY- Patent dated June-l3, 1905.- Disclaimer filed January 24, 1906, by the patentee.
Enters his disclaimer- To claim- No. 1, which reads as follows, to wit: a
1. The process of electrodepositing antimony which consists in .electroly'zing a --triflnorid with a suitable cathode.-[Ofiim'al Gazette
US20894404A 1904-05-20 1904-05-20 Process of electrodepositing antimony. Expired - Lifetime US792307A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US20894404A US792307A (en) 1904-05-20 1904-05-20 Process of electrodepositing antimony.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US20894404A US792307A (en) 1904-05-20 1904-05-20 Process of electrodepositing antimony.

Publications (1)

Publication Number Publication Date
US792307A true US792307A (en) 1905-06-13

Family

ID=2860796

Family Applications (1)

Application Number Title Priority Date Filing Date
US20894404A Expired - Lifetime US792307A (en) 1904-05-20 1904-05-20 Process of electrodepositing antimony.

Country Status (1)

Country Link
US (1) US792307A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2441810A (en) * 1943-01-01 1948-05-18 Rca Corp Phototube and method of manufacture
US2515192A (en) * 1944-09-27 1950-07-18 Poor & Co Method of electroplating
US2634235A (en) * 1946-06-21 1953-04-07 Olin Ind Inc Lead-antimony alloy electroplating bath
US2715096A (en) * 1953-01-22 1955-08-09 Rca Corp Antimony plating
US2721836A (en) * 1952-08-07 1955-10-25 Harshaw Chem Corp Electrodeposition of antimony

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2441810A (en) * 1943-01-01 1948-05-18 Rca Corp Phototube and method of manufacture
US2515192A (en) * 1944-09-27 1950-07-18 Poor & Co Method of electroplating
US2634235A (en) * 1946-06-21 1953-04-07 Olin Ind Inc Lead-antimony alloy electroplating bath
US2721836A (en) * 1952-08-07 1955-10-25 Harshaw Chem Corp Electrodeposition of antimony
US2715096A (en) * 1953-01-22 1955-08-09 Rca Corp Antimony plating

Similar Documents

Publication Publication Date Title
US4085016A (en) Method and apparatus for the oxidation of organic material present in concentrated sulfuric acid
US2828251A (en) Electrolytic cladding process
US2872405A (en) Lead dioxide electrode
JPH03504616A (en) Electrolytic manufacturing method for polyvalent metals and equipment for carrying out this electrolytic manufacturing method
US2786809A (en) Electrolytic cladding
US3423300A (en) Electrolytic regeneration of reduced chromium compounds
US3497425A (en) Electrodes and methods of making same
US1077920A (en) Electrode.
US792307A (en) Process of electrodepositing antimony.
US3928153A (en) Electrowinning process
Narasimham et al. Preparation and applications of graphite substrate lead dioxide (GSLD) anode
US1465034A (en) Process for the electrolytic deposition of copper
US2975111A (en) Production of titanium
US3301777A (en) Anode for the electrowinning of manganese
US6432293B1 (en) Process for copper-plating a wafer using an anode having an iridium oxide coating
US3855089A (en) Process for the electrolytic refining of heavy metals
US3200055A (en) Process for the electrolytic production of hyperpure zinc
US902755A (en) Electrolyte for electroplating.
US3493478A (en) Electrolytic preparation of perchlorates
US2782156A (en) Purification of fused salt electrolytes
US789523A (en) Process of electrolytically refining copper-nickel alloys.
US1127966A (en) Deposition of iron.
US2623848A (en) Process for producing modified electronickel
US2457021A (en) Palladium plating
EP0033956B1 (en) Stable lead dioxide anode and method for production