US1055653A - Electrolytic process. - Google Patents

Electrolytic process. Download PDF

Info

Publication number
US1055653A
US1055653A US701297A US1912701297A US1055653A US 1055653 A US1055653 A US 1055653A US 701297 A US701297 A US 701297A US 1912701297 A US1912701297 A US 1912701297A US 1055653 A US1055653 A US 1055653A
Authority
US
United States
Prior art keywords
lead
anode
solution
sulfate
spongy
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
US701297A
Inventor
Charles J Reed
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 US701297A priority Critical patent/US1055653A/en
Application granted granted Critical
Publication of US1055653A publication Critical patent/US1055653A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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
    • C25D3/12Electroplating: Baths therefor from solutions of nickel or cobalt

Definitions

  • Cobalt has the same property as zinc of being unreduced and unaffected in solution as sulfate by contact with metallic lead. I find that. an anode of spongy lead may be used to combine with the (S0,) of the sulfate of this metal to produce insoluble sulfate of lead and prevent the liberation of free sulfuric acid in the electrolyte. This enables me to electrolytically deposit the metal from its sulfate solution without the inetllcicncy due to the presence of free sulfuric acid.
  • anode of spongy lead as herein used, I do not mean that the entire electrode consists neccssarll otlepongy lead, but only that it contains spongy lead chemically-active materials. It may, for example, be made up of a conducting framemi-a of hard load, antimonial lead or other suitable material capable of conducting the electric current and having spongy lead a plied to or contained in it, as in the or inary accumulator plate.

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 Metals (AREA)

Description

HEB @TATES rarest curios;
CHARLES 3'. REED, 0F PHILADELPHIA, PENNSYLVANIA.
ELECTROLYTIC PROCESS.
filed June 3, 1912.
To all whom it mag concern:
Be it known that I, CHAiiLiis J. REE a citizen of the United States, residing at Philadelphia, in the county of Philadelphia and State of Pennsylvania, have invented percentage of free acid in too solution increases, the deposition of the metal with a given current. decreases. This difiiculty was overcome in the case of zinc by a process described by Carl llcring J. Letters Patent No. 798,790, granted September 5, 1905.
Cobalt has the same property as zinc of being unreduced and unaffected in solution as sulfate by contact with metallic lead. I find that. an anode of spongy lead may be used to combine with the (S0,) of the sulfate of this metal to produce insoluble sulfate of lead and prevent the liberation of free sulfuric acid in the electrolyte. This enables me to electrolytically deposit the metal from its sulfate solution without the inetllcicncy due to the presence of free sulfuric acid.
ln the operation of my process, I prepare a. solution of the sulfate'ot cobalt and elec: trolyze it. with a cathode of any suitable conducting substance, such as carbon, copper, aluminum or any conducting body on which it is desired to dcposi the cobalt, and an anode of spongy or finely-divided lead, such as is usually employed in the negative plates of a lead accumulator. The sum of the reactions which take place may be represented by the following chemical equation:
Flint-C030,:Co-l-PbSU This means that the metallic lead combines with the S0, of the cobalt sulfate and the cobalt is set free in the metallic state, there being no other chemical changes in the solii- Specification of Letters Patent.
this application Serial No. 701,297.
practice in the discharge of an accumulaton When this has occurred I remove the anode (replacing it with a fresh one) and place it in a dilute solution of sulfuric acid and passan electric current through it in'the opposite direction, using it as a cathode until the lead sulfate has all or nearly all been reduced to metallic spongy lead and the SO, liberated as sulfuric acid. The electroden ay then be again used as an anode in the deposition cell and the operation becomes cyclic, the sulfuric acid being a icy-product which may be recovered and utilized.
1 do not limit myself to the use of any particular substance as a cathode for receiving the of nickel or aluminum.
By the term anode of spongy lead as herein used, I do not mean that the entire electrode consists neccssarll otlepongy lead, but only that it contains spongy lead chemically-active materials. It may, for example, be made up of a conducting framemi-a of hard load, antimonial lead or other suitable material capable of conducting the electric current and having spongy lead a plied to or contained in it, as in the or inary accumulator plate.
This application is'a division of Serial sists in elcctrolyzing said solution, using an anode of spongy lead, and subsequently re generating said anode material in a-sepa rate receptacle, substantially as herein de,
scribed. Y
3. The process of reducing metallic-foo,-
baltfrom its solution as sulfate, which 'con-' sists in electrolyzing said solution,.ii'sing an anode of spongy lead, endelectrolytically regenerating said anode-materialin a, sepa Patented Mar. it, 191%. No Drawing. Original application filed May 10, 1911, Serial No. 326,148. Divided and deposit of cobalt, but, prefer a sheet a spongy lead, substantially as j all 3 consists in electrolyzing said solution, using rate receptacle, substantially as herein set acid as a by-product, substantially as herein forth. 1 described. 10
4. The process of recovering metallic 00- In testimony whereof I affix my signature balt from a solution of its sulfate, which in presence of two Witnesses.
CHARLES J. REED. an anode of spongy lead, electrolytically 1e-' Witnesses:
generating'saicl anode material in a sepa- FRANK A. LEACH, rate receptacle, and recovering the sulfuric J. M. JACKSON.
US701297A 1911-05-10 1912-06-03 Electrolytic process. Expired - Lifetime US1055653A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US701297A US1055653A (en) 1911-05-10 1912-06-03 Electrolytic process.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US1911626148A 1911-05-10 1911-05-10
US701297A US1055653A (en) 1911-05-10 1912-06-03 Electrolytic process.

Publications (1)

Publication Number Publication Date
US1055653A true US1055653A (en) 1913-03-11

Family

ID=3123911

Family Applications (1)

Application Number Title Priority Date Filing Date
US701297A Expired - Lifetime US1055653A (en) 1911-05-10 1912-06-03 Electrolytic process.

Country Status (1)

Country Link
US (1) US1055653A (en)

Similar Documents

Publication Publication Date Title
US2631115A (en) Electrodes for electrochemical cells
JPS62230994A (en) Electrolytic recovery of lead from scrap
US3068157A (en) Process for using the decomposition energy of amalgams for electrolysis of metal salts by using reversible hydrogen electrodes
US1662866A (en) Secondary battery or accumulator
US4064022A (en) Method of recovering metals from sludges
US1032623A (en) Electrolytic process.
US1055653A (en) Electrolytic process.
US1942791A (en) Electrode for secondary cells
US1055652A (en) Electrolytic process.
US528648A (en) Charles j
US1077894A (en) Electrode.
US436602A (en) William b
US1299414A (en) Electrolytic refining of metallic zinc-bearing materials.
US938451A (en) Process of making active material for storage-battery electrodes.
US307945A (en) William s
US1632307A (en) Peroxide of lead, zinc, and sulphuric-acid accumulators
US862871A (en) Process of reducing metallic sulfids.
US565953A (en) Emile andreoli
US2156222A (en) Counterelectromotive-force cell
US2532629A (en) Method of electrodepositing iron
US738719A (en) Galvanic cell.
US719871A (en) Electrolytic apparatus.
US719870A (en) Electrolytic apparatus.
US798790A (en) Electrolytic process.
US598193A (en) Emile andreoli