[go: up one dir, main page]

US1397008A - Method of preparing finely-divided metals - Google Patents

Method of preparing finely-divided metals Download PDF

Info

Publication number
US1397008A
US1397008A US254346A US25434618A US1397008A US 1397008 A US1397008 A US 1397008A US 254346 A US254346 A US 254346A US 25434618 A US25434618 A US 25434618A US 1397008 A US1397008 A US 1397008A
Authority
US
United States
Prior art keywords
metal
anode
cathode
oleaginous
metals
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
US254346A
Inventor
Mcgall Albert
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 US254346A priority Critical patent/US1397008A/en
Application granted granted Critical
Publication of US1397008A publication Critical patent/US1397008A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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

Definitions

  • This invention is an electrolytic method whereby oxidizable metals, such for example as zinc, copper, aluminum, etc., may be prepared in a state of minute subdivision but in non-oxidized condition.
  • oxidizable metals such for example as zinc, copper, aluminum, etc.
  • the metals so prepared are useful for a wide variety of purposes, among which may be mentioned the preparation of electrodes for primary or secondary batteries, and the manufacture of explosives of the known type comprising a metallic component and an oxidizing agent, such for example as ammonium nitrate.
  • Sheet zinc which has preferably been amalgamated (although this is not essential) is coated by rubbing or otherwise with a thln layer of a suitable oleaginous substance, such for example as an organic or inorgan c (hydrocarbon) oil or grease, or material containing the same.
  • a suitable oleaginous substance such for example as an organic or inorgan c (hydrocarbon) oil or grease, or material containing the same.
  • the coated sheet is then connected as the anode in a suitable electrolyte, which is preferably acid, and may consist initially of a sulfuric acid solution having a specific gravity of about 1.3.
  • a suitable cathode is provided which is preferably also of zinc: for although other metallic or conductive materials may be employed as cathode, there is less liability to loss of metal by local action when zinc is used.
  • the coating of the cathode is, however, a distinct advantage for the reason that the cathode, if provided with an oleaginous coating, is not acted upon by the electrolyte when the flow of current is interrupted.
  • Unidirectional current from an outside source is then caused to flow from the coated sheet zinc as anode, whereupon, irrespective of the current density employed, a deposit of sponge or minutely subdivided zinc will be formed.
  • This deposit is at most only loosely adherent to the cathode, and may be either continuously or intermittently removed from the electrolyte, washed and dried.
  • a current density of about one ampere per square inch of cathode surface will be found satisfactory; and the anode and cathode areas may be substantially equal.
  • the coated metal although quite unafiected by the acid electrolyte so long as no current flows through the system, nevertheless passes freely into solution as soon as current is applied from an external source, and is simultaneously deposited in minutely subdivided or sponge form at the cathode.
  • the deposit will be found to be substantially non-oxidized, and relatively very stable. This I now attribute to the presence upon the individual particles of the deposit of an oleaginous protective coating of extreme tenuity.
  • Finely subdivided copper is readily prepared under the above conditions.
  • Metallic aluminum in minute subdivision may also be prepared in substantially the same manner.
  • the aluminum deposit is however more liable to oxidation than zinc when removed from the solution, and especially when spread in contact with air. Consequently the aluminum deposit should preferably be shielded to a reasonable degree from oxidizing influences, as for example by storing in an inert atmosphere, or even by compressing in order to reduce the exposed surface.
  • immunized metals which have been treated with an oleaginous material and thereby rendered in active toward acid electrolytes so long as no current flows through an electric circuit in which they may be included as anode, are conveniently referred to as immunized metals
  • the immunity from purely chemi cal as distinguished from electrochemical attack thus conferred is remarkably persistent; and, particularly in the case of electrodes which have been in use for some time, may persist after thorough wiping of the electrode, and even after washing it with such cleansing agents as gasolene, etc., until all apparent traces of the oleaginous coating have been removed.
  • metal is used herein to include alloys, to which the method is likewise applicable.
  • I claim 1 Method of preparing oXidizable metals in minutely subdivided, non-oxidizedcondition, comprising electrodepositing the metal in sponge form by means of an electric current flowing from an immunized metal anode.
  • Method of preparing oXidizable metals in minutely subdivided, non-oxidized condition comprising electrodepositing the metal in sponge form by means of an electric current flowing from an anode of the same metal, said anode presenting surfaces having an oleaginous coating.
  • Method of preparing oxidizable metals in minutely subdivided, non-oxidized condition comprising electrodepositing the metal in sponge form by means of an electric current passing between an anode and cathode of the desired metal, said anode immunized by treatment with an oleaginous substance.
  • Method of preparing oXidizable metals in minutely sudivided, non-oxidized condition comprising electrodepositing the metal in sponge form by means of an electric current passing between an anode and cathode of the desired metal, both of said electrodes immunized by treatment with an oleaginous substance.

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

UNITED STATES PATENT OFFICE.
ALBERT MCG'ALL, OF NEW YORK, N. Y.
No Drawing. Application filed September 16, 1918, Serial No. 254,346.
Specification of Letters Patent.
Patented Nov. 15, 1921.
Renewed February 2, 1921.
Serial No. 442,012.
To all whom it may concern Be it known that I, ALBERT MoGALL, a citizen of the United States, residing at New York, in the county of New York and State of New York, have invented certain new and useful Improvements in Methods of Preparing Finely-Divided Metals, of which the following is a specification.
This invention is an electrolytic method whereby oxidizable metals, such for example as zinc, copper, aluminum, etc., may be prepared in a state of minute subdivision but in non-oxidized condition. The metals so prepared are useful for a wide variety of purposes, among which may be mentioned the preparation of electrodes for primary or secondary batteries, and the manufacture of explosives of the known type comprising a metallic component and an oxidizing agent, such for example as ammonium nitrate.
I will describe my invention by reference to the preparation of non-oxidized zinc in minutely sudivided state, as a typical or illustrative example thereof. It will be understood, however, that the invention is not restricted to the particular manipulative details below described, since the composition and concentration of the electrolyte, as well as the current conditions, may be rather widely varied. Obviously also the conditions will be somewhat varied according to the particular metal which it is desired to obtain in subdivided form.
I prefer to proceed as follows:
Sheet zinc, which has preferably been amalgamated (although this is not essential) is coated by rubbing or otherwise with a thln layer of a suitable oleaginous substance, such for example as an organic or inorgan c (hydrocarbon) oil or grease, or material containing the same. The mineral grease known to the trade as sponge grease, and having the characteristics of a non-flowing grease or oil, is entirely satisfactory for my purposes.
The coated sheet is then connected as the anode in a suitable electrolyte, which is preferably acid, and may consist initially of a sulfuric acid solution having a specific gravity of about 1.3. A suitable cathode is provided which is preferably also of zinc: for although other metallic or conductive materials may be employed as cathode, there is less liability to loss of metal by local action when zinc is used. Also, I prefer to apply a like oleaginous coating to the cathode although this is not necessary for the practice of the invention. The coating of the cathode is, however, a distinct advantage for the reason that the cathode, if provided with an oleaginous coating, is not acted upon by the electrolyte when the flow of current is interrupted.
Unidirectional current from an outside source is then caused to flow from the coated sheet zinc as anode, whereupon, irrespective of the current density employed, a deposit of sponge or minutely subdivided zinc will be formed. This deposit is at most only loosely adherent to the cathode, and may be either continuously or intermittently removed from the electrolyte, washed and dried. A current density of about one ampere per square inch of cathode surface will be found satisfactory; and the anode and cathode areas may be substantially equal.
Contrary to what might be anticipated from the known insulating character of oleaginous materials, it will be found that the coated metal, although quite unafiected by the acid electrolyte so long as no current flows through the system, nevertheless passes freely into solution as soon as current is applied from an external source, and is simultaneously deposited in minutely subdivided or sponge form at the cathode. Instead, however, of forming a highly oxidizable, unstable, and often partially oxidized sponge, as is the case when the oleaginous coating is omitted, the deposit will be found to be substantially non-oxidized, and relatively very stable. This I now attribute to the presence upon the individual particles of the deposit of an oleaginous protective coating of extreme tenuity.
Finely subdivided copper is readily prepared under the above conditions. Metallic aluminum in minute subdivision may also be prepared in substantially the same manner. The aluminum deposit is however more liable to oxidation than zinc when removed from the solution, and especially when spread in contact with air. Consequently the aluminum deposit should preferably be shielded to a reasonable degree from oxidizing influences, as for example by storing in an inert atmosphere, or even by compressing in order to reduce the exposed surface.
Metals which have been treated with an oleaginous material and thereby rendered in active toward acid electrolytes so long as no current flows through an electric circuit in which they may be included as anode, are conveniently referred to as immunized metals The immunity from purely chemi cal as distinguished from electrochemical attack thus conferred is remarkably persistent; and, particularly in the case of electrodes which have been in use for some time, may persist after thorough wiping of the electrode, and even after washing it with such cleansing agents as gasolene, etc., until all apparent traces of the oleaginous coating have been removed. I employ the expression immunized metal anode in the claims to designate anodes possessing the above described characteristic due to the previous treatment with oil or equivalent material.
The term metal is used herein to include alloys, to which the method is likewise applicable.
I claim 1. Method of preparing oXidizable metals in minutely subdivided, non-oxidizedcondition, comprising electrodepositing the metal in sponge form by means of an electric current flowing from an immunized metal anode.
2. Method of preparing oXidizable metals in minutely subdivided, non-oxidized condition, comprising electrodepositing the metal in sponge form by means of an electric current flowing from an anode of the same metal, said anode presenting surfaces having an oleaginous coating.
3. Method of preparing oxidizable metals in minutely subdivided, non-oxidized condition, comprising electrodepositing the metal in sponge form by means of an electric current passing between an anode and cathode of the desired metal, said anode immunized by treatment with an oleaginous substance.
4. Method of preparing oXidizable metals in minutely sudivided, non-oxidized condition, comprising electrodepositing the metal in sponge form by means of an electric current passing between an anode and cathode of the desired metal, both of said electrodes immunized by treatment with an oleaginous substance.
In testimony whereof, I aflix my signature.
ALBERT MoGALL.
US254346A 1918-09-16 1918-09-16 Method of preparing finely-divided metals Expired - Lifetime US1397008A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US254346A US1397008A (en) 1918-09-16 1918-09-16 Method of preparing finely-divided metals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US254346A US1397008A (en) 1918-09-16 1918-09-16 Method of preparing finely-divided metals

Publications (1)

Publication Number Publication Date
US1397008A true US1397008A (en) 1921-11-15

Family

ID=22963937

Family Applications (1)

Application Number Title Priority Date Filing Date
US254346A Expired - Lifetime US1397008A (en) 1918-09-16 1918-09-16 Method of preparing finely-divided metals

Country Status (1)

Country Link
US (1) US1397008A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4676877A (en) * 1984-03-16 1987-06-30 Societe de Promotion des Procedes Hydro-Metallurgiques Process for production of fine and ultrafine zinc powders by electrolysis in a basic medium
US20040074627A1 (en) * 2002-10-17 2004-04-22 Ravi Verma Method for processing of continuously cast aluminum sheet
US20040108200A1 (en) * 2002-09-12 2004-06-10 Des Jardins Stephen R. Controlled concentration electrolysis system
US20040140222A1 (en) * 2002-09-12 2004-07-22 Smedley Stuart I. Method for operating a metal particle electrolyzer
US20040168922A1 (en) * 2002-09-12 2004-09-02 Smedley Stuart I. Discrete particle electrolyzer cathode and method of making same
US20050098442A1 (en) * 2002-09-12 2005-05-12 Smedley Stuart I. Method of production of metal particles through electrolysis

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4676877A (en) * 1984-03-16 1987-06-30 Societe de Promotion des Procedes Hydro-Metallurgiques Process for production of fine and ultrafine zinc powders by electrolysis in a basic medium
US20040108200A1 (en) * 2002-09-12 2004-06-10 Des Jardins Stephen R. Controlled concentration electrolysis system
US20040140222A1 (en) * 2002-09-12 2004-07-22 Smedley Stuart I. Method for operating a metal particle electrolyzer
US20040168922A1 (en) * 2002-09-12 2004-09-02 Smedley Stuart I. Discrete particle electrolyzer cathode and method of making same
US20050098442A1 (en) * 2002-09-12 2005-05-12 Smedley Stuart I. Method of production of metal particles through electrolysis
US7166203B2 (en) 2002-09-12 2007-01-23 Teck Cominco Metals Ltd. Controlled concentration electrolysis system
US7273537B2 (en) 2002-09-12 2007-09-25 Teck Cominco Metals, Ltd. Method of production of metal particles through electrolysis
US7470351B2 (en) 2002-09-12 2008-12-30 Teck Cominco Metals Ltd. Discrete particle electrolyzer cathode and method of making same
US20040074627A1 (en) * 2002-10-17 2004-04-22 Ravi Verma Method for processing of continuously cast aluminum sheet

Similar Documents

Publication Publication Date Title
Frankenthal et al. The anodic corrosion of gold in concentrated chloride solutions
US3118828A (en) Electrode structure with titanium alloy base
US3663379A (en) Method and electrolytes for anodizing titanium and its alloys
US2446349A (en) Electrodeposition of aluminum
Vermilyea Conduction and rectification in anodic oxide films
JPH035024B2 (en)
US2221596A (en) Method of manufacturing dry rectifiers
US1397008A (en) Method of preparing finely-divided metals
US3489539A (en) Manganiding
US4659629A (en) Formation of a protective outer layer on magnesium alloys containing aluminum
US3845364A (en) Cathode electrode for operation under conditions of reverse polarity voltage
US3190822A (en) Process for electrolytically etching valve metal surfaces
JPS5825083A (en) Manufacturing method for zinc powder electrodes for primary batteries
US3684577A (en) Removal of conductive coating from dimensionally stable electrodes
US3378471A (en) Anodized tantalum and niobium and method of forming an oxide coating thereon
DE2437183A1 (en) ALKALINE BATTERY
US3259475A (en) Etched metal valve surfaces of tantalum or niobium or titanium
US3063917A (en) Anodic decontamination of zirconium and hafnium
US2871424A (en) Electrolytic capacitor
US3321389A (en) Method of anodically etching aluminum foils at elevated temperatures in an electrolyte including chloride and sulfate ions
US2997429A (en) Electropolishing of titanium and titanium alloys
US1922847A (en) Process of metal deposition and product thereof
US2794775A (en) Electroplating with tungsten
US1684684A (en) Electrolytic rectifier
Benjamin et al. The deposition of oxide coatings by cataphoresis