[go: up one dir, main page]

US713278A - Electrodeposited lead. - Google Patents

Electrodeposited lead. Download PDF

Info

Publication number
US713278A
US713278A US12657602A US1902126576A US713278A US 713278 A US713278 A US 713278A US 12657602 A US12657602 A US 12657602A US 1902126576 A US1902126576 A US 1902126576A US 713278 A US713278 A US 713278A
Authority
US
United States
Prior art keywords
lead
electrolyte
electrodeposited
electrolysis
density
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
US12657602A
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 US12657602A priority Critical patent/US713278A/en
Application granted granted Critical
Publication of US713278A publication Critical patent/US713278A/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
    • C25D3/34Electroplating: Baths therefor from solutions of lead
    • C25D3/36Electroplating: Baths therefor from solutions of lead characterised by the organic bath constituents used

Definitions

  • ANsoN GARDER isnr'rs, oF LANSINGBURG, NEW YORK.
  • the present invention relates to a lead prod-I uct obtained by electrolysis.
  • the lead resulting from electrolysis by methods heretofore commonly employed is characterized by lack of density,incoherency, and by a crystalline spongy'formation, rendering the electrodeposit unsuitable for fusion.
  • the object of my invention is to produce by electrolytic treatment substantially pure lead having substantially the density and homogeneity of cast lead. Such object is attained by the employment in connection with a suitable electrolyte of an agent capable of restraining the crystallization of the deposit.
  • a suitable electrolyte such as, for example, a solution of a lead salt of Iiuorin acid-as described in United States Letters Patent No. 679,824, granted to me August 6, 1901.
  • a reducing agent which I have found gives adeposit characterized as herein described.
  • substances which I have found available for such purposes are: gelatin, pyrogallol, resorcinol, saligenin, orthoamidophenol, hydroquinone, and sulfurous acid. Phenols of the aromatic series are well adapted for use in the present process by reason of their being easily oxidizable. The characteristics of the electrodeposit are believed to be due to the reducing action of the agent employed.
  • the agent contained in the electrolyte serves to restrain the crystallization of the electrodeposited lead and causes the same to form at or upon the cathode in a solid coherent body of substantially uniform structure throughout having substantially the density and homogeneity of cast lead,con stituting a product which by reason of its physical properties facilitates the practical electrolytic refining operations and which may be fused without the formation of an un due amount of dross.
  • l I am able to produce without mechanical treatment a deposit that can be made of considerable thickness and which is non-porous, as shown by the specilic gravity of a mass of it.
  • a product is easily made with a specic gravity of'1l.36, the same metal remelted and cast having the same density.
  • gelatin the cheapest and to give the best results and prefer its use in the proportion of one part of gelatin, by weight, to five thousand parts of solution.
  • the current efficiency does not appear to be affected bythe presence of gelatin or of any of the othe'rnamed agents in the electrolyte.
  • the agent may be applied to the electrolyte in such quantities as desired from time to time. If gelatin is used, it is dissolved in hot Water and a suiiicientquantity of this solution added to the electrolyte so as to make the desired proportion.
  • the product of the method described is superior to VLead products of prior processes for remelting and for maintaining without attention the proper conditions of work in the electrolytic retining-tanks-that is,without shortcircuiting.
  • the electrodeposit is not mechanically treated while being formed by the present process, it retains undisturbed the normal structural characteristics due to electrolysis.
  • the appearance of the surface of the deposit changes as the electrolysis proceeds, beginning with a frosty7 appearance and becoming coarser until it has a pebbly or botryoidal appearance.
  • FIG. 1 is a vertical cross-section of the apparatus employed in treating lead by my improved process.
  • Fig. 2 is a plan view of a metallic plate electroplated with lead by my improved process, the plate being partly broken away.
  • Fig. 3 is a vertical cross-section of the same.
  • the anode consists of lead or lead alloy to be refined.
  • the cathode is shown of a metallic plate suspended in position to receive the deposited lead.
  • electrodeposited lead characterized by substantial purity, cohereucy, uniformity of structure throughout, and having substantially the density and homogeneity of cast lead.
  • electrodeposited lead characterized by substantial purity, coherency and uniformity of structure throughout, practically free from crystallization, and having substantially the homogeneity, with a density of about 11.3, and retaining the normal structural characteristics due to electrolysis.

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

No. 713,278. Patented Nov. ll, |902;
' A. G. BETTs.
L ECTBODEPOSITED LEAD.
(Application filed Oct. 9, 1902.)
.(Nn Moden) tlNiTED STATES PAJLRNLOFFICE.
ANsoN GARDER isnr'rs, oF LANSINGBURG, NEW YORK.
ELECTRODEPOSITED LEAD.
SPECIFICATION forming part of Letters'Patent No. 713,278, dated November 11, 1902. Application filed 0otober9, 1902. Serial No. 1261576. (N0 Specimens.)
To all whom it may concern:
Be it known that I, ANsoN GARDNER BE'rTs,
The present invention relates to a lead prod-I uct obtained by electrolysis.
The lead resulting from electrolysis by methods heretofore commonly employed is characterized by lack of density,incoherency, and by a crystalline spongy'formation, rendering the electrodeposit unsuitable for fusion.
The object of my invention is to produce by electrolytic treatment substantially pure lead having substantially the density and homogeneity of cast lead. Such object is attained by the employment in connection with a suitable electrolyte of an agent capable of restraining the crystallization of the deposit.
To carry ont my invention, I employ a suitable electrolyte-such as, for example, a solution of a lead salt of Iiuorin acid-as described in United States Letters Patent No. 679,824, granted to me August 6, 1901. To the electrolyte is added a quantity of a reducing agent, which I have found gives adeposit characterized as herein described. Among the substances which I have found available for such purposes are: gelatin, pyrogallol, resorcinol, saligenin, orthoamidophenol, hydroquinone, and sulfurous acid. Phenols of the aromatic series are well adapted for use in the present process by reason of their being easily oxidizable. The characteristics of the electrodeposit are believed to be due to the reducing action of the agent employed.
The agent contained in the electrolyte, as above stated, serves to restrain the crystallization of the electrodeposited lead and causes the same to form at or upon the cathode in a solid coherent body of substantially uniform structure throughout having substantially the density and homogeneity of cast lead,con stituting a product which by reason of its physical properties facilitates the practical electrolytic refining operations and which may be fused without the formation of an un due amount of dross. By the present process l I am able to produce without mechanical treatmenta deposit that can be made of considerable thickness and which is non-porous, as shown by the specilic gravity of a mass of it. A product is easily made with a specic gravity of'1l.36, the same metal remelted and cast having the same density. I have observed with some of the more active of these agents,as gelatin and pyrogallol,the projections that always occur on thick electrodeposits are nodular, while with some of the weaker agents, as orthoamidophenol and saligenin,the projections are apt to be crystals. When the projections are nodular,they swell into lumps on the surface during electrolysis,reducing the liability of short-circuiting during practical working of the process. With the crystalline form of projection shortcircuiting occurs, rendering such deposits less desirable or suitable for electrolytic refining or electroplating, although the deposit is superior to that obtained by prior electrolytic processes. There appears to be a very slight increasein the weight of the lead deposit in connection with the use of the above agents. These agents also affect to sonne extent the solution of lead at the anode by preserving the mass of solid lead underneath the anode slime with a somewhat smoother surface.
In practicing my present invention I prefer a current strength of ten to twenty amperes per square foot of cathode surface and a corresponding tension of .15 to .35 volts for each element. With higher currents the lead becomes harder and more brittle and takes on a whitishcolor and silvery luster. A sample deposited with a current of forty amperes per square foot showed a specific gravity of 11.276. In general the deposited lead is apt to be slightly stiffer than ordinary lead; but this stiffness may be regulated at will by varying the current density and the quantity of agent in the solution.
Of the above-named agents I have found gelatin the cheapest and to give the best results and prefer its use in the proportion of one part of gelatin, by weight, to five thousand parts of solution. The current efficiency does not appear to be affected bythe presence of gelatin or of any of the othe'rnamed agents in the electrolyte. The agent may be applied to the electrolyte in such quantities as desired from time to time. If gelatin is used, it is dissolved in hot Water and a suiiicientquantity of this solution added to the electrolyte so as to make the desired proportion.
The product of the method described is superior to VLead products of prior processes for remelting and for maintaining without attention the proper conditions of work in the electrolytic retining-tanks-that is,without shortcircuiting. As the electrodeposit is not mechanically treated while being formed by the present process, it retains undisturbed the normal structural characteristics due to electrolysis. The appearance of the surface of the deposit changes as the electrolysis proceeds, beginning with a frosty7 appearance and becoming coarser until it has a pebbly or botryoidal appearance.
Any suitable electrolylic apparatus may be employed to carry out the present process. I have shown one form of apparatus in the accompanying drawings, in which- Figure 1 is a vertical cross-section of the apparatus employed in treating lead by my improved process. Fig. 2 is a plan view of a metallic plate electroplated with lead by my improved process, the plate being partly broken away. Fig. 3 is a vertical cross-section of the same.
1 is the electrolytic vat containing the electrolyte 2, with a restraining agent, as above described.
3 is the anode, and 4 the cathode, suspended in the electrolyte and connected with the respective poles of an electric energizer. (Not shown.) The anode consists of lead or lead alloy to be refined. The cathode is shown of a metallic plate suspended in position to receive the deposited lead.
represents the electrodeposited lead, having the characteristics above described.
I claim and desire to obtain by Letters Patent the following:
1. As a new product, electrodeposited lead characterized by substantial purity, cohereucy, uniformity of structure throughout, and having substantially the density and homogeneity of cast lead.
2. As a new product, electrodeposited lead characterized by substantial purity, coherency and uniformity of structure throughout, practically free from crystallization, and having substantially the homogeneity, with a density of about 11.3, and retaining the normal structural characteristics due to electrolysis.
3. As a new product electrodeposited lead formed by subjecting to electrolysis an electrolyte containing in solution a lead salt ofa fluorin acid and a reducing agent.
In testimony whereof I have signed this specification in the presence of two subscribing witnesses.
ANSON GARDNER BETTS.
Witnesses:
EDGAR H. BETTS, S. D. NICHOLS.
US12657602A 1902-10-09 1902-10-09 Electrodeposited lead. Expired - Lifetime US713278A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US12657602A US713278A (en) 1902-10-09 1902-10-09 Electrodeposited lead.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US12657602A US713278A (en) 1902-10-09 1902-10-09 Electrodeposited lead.

Publications (1)

Publication Number Publication Date
US713278A true US713278A (en) 1902-11-11

Family

ID=2781800

Family Applications (1)

Application Number Title Priority Date Filing Date
US12657602A Expired - Lifetime US713278A (en) 1902-10-09 1902-10-09 Electrodeposited lead.

Country Status (1)

Country Link
US (1) US713278A (en)

Similar Documents

Publication Publication Date Title
US4652348A (en) Method for the production of alloys possessing high elastic modulus and improved magnetic properties by electrodeposition
JP4221064B2 (en) Electrodeposition method of copper layer
JPS59100283A (en) Metal products and manufacture
US3576724A (en) Electrodeposition of rutenium
US4391679A (en) Electrolytic bath and process for the deposition of gold alloy coatings
US2541721A (en) Process for replenishing nickel plating electrolyte
US1465034A (en) Process for the electrolytic deposition of copper
US4439284A (en) Composition control of electrodeposited nickel-cobalt alloys
US1566265A (en) Process of producing electrolytic copper
US3864227A (en) Method for the electrolytic refining of copper
US713278A (en) Electrodeposited lead.
US713277A (en) Electrolytic refining of lead and lead alloys.
US3522155A (en) Method of electrodepositing a tinbismuth alloy and compositions therefor
US3799850A (en) Electrolytic process of extracting metallic zinc
US805969A (en) Separation of metals.
USRE12117E (en) Electrodeposxted lead
US570554A (en) Eduard jordis
US2489523A (en) Electrodeposition of tin or lead-tin alloys
US3437571A (en) Production of electrolytic nickel
US2457021A (en) Palladium plating
US1857664A (en) Treatment of gold and silver
US1127966A (en) Deposition of iron.
USRE12301E (en) Process of electrolytically refining lead
JP3158684B2 (en) Copper electrorefining method
US3374154A (en) Electroforming and electrodeposition of stress-free nickel from the sulfamate bath