US2895889A - Low stress electrodeposited rhodium - Google Patents

Low stress electrodeposited rhodium Download PDF

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Publication number
US2895889A
US2895889A US633381A US63338157A US2895889A US 2895889 A US2895889 A US 2895889A US 633381 A US633381 A US 633381A US 63338157 A US63338157 A US 63338157A US 2895889 A US2895889 A US 2895889A
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US
United States
Prior art keywords
rhodium
bath
per liter
stress
electrodeposited
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
US633381A
Inventor
Schumpelt Karl
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.)
SEL REX PRECIOUS METALS Inc
SEL-REX PRECIOUS METALS Inc
Occidental Chemical Corp
Original Assignee
SEL REX PRECIOUS METALS Inc
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
Priority to DENDAT1068081D priority Critical patent/DE1068081B/de
Priority to NL111673D priority patent/NL111673C/xx
Priority to DENDAT1072047D priority patent/DE1072047B/en
Application filed by SEL REX PRECIOUS METALS Inc filed Critical SEL REX PRECIOUS METALS Inc
Priority to US633381A priority patent/US2895889A/en
Priority to US663595A priority patent/US2895890A/en
Priority to GB31318/57A priority patent/GB836475A/en
Priority to GB38673/57A priority patent/GB835830A/en
Priority to CH5393857A priority patent/CH378635A/en
Priority to FR1189477D priority patent/FR1189477A/en
Priority to FR759094A priority patent/FR72983E/en
Priority to CH5685658A priority patent/CH418084A/en
Application granted granted Critical
Publication of US2895889A publication Critical patent/US2895889A/en
Anticipated expiration legal-status Critical
Assigned to HOOKER CHEMICALS & PLASTICS CORP. reassignment HOOKER CHEMICALS & PLASTICS CORP. MERGER (SEE DOCUMENT FOR DETAILS). Assignors: OXY METAL INDUSTRIES CORPORATION
Assigned to OCCIDENTAL CHEMICAL CORPORATION reassignment OCCIDENTAL CHEMICAL CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). EFFECTIVE MARCH 30, 1982. Assignors: HOOKER CHEMICAS & PLASTICS CORP.
Expired - Lifetime legal-status Critical Current

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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
    • C25D3/50Electroplating: Baths therefor from solutions of platinum group metals
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J19/00Details of vacuum tubes of the types covered by group H01J21/00
    • H01J19/28Non-electron-emitting electrodes; Screens
    • H01J19/30Non-electron-emitting electrodes; Screens characterised by the material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01JELECTRIC DISCHARGE TUBES OR DISCHARGE LAMPS
    • H01J2893/00Discharge tubes and lamps
    • H01J2893/0001Electrodes and electrode systems suitable for discharge tubes or lamps
    • H01J2893/0012Constructional arrangements
    • H01J2893/0019Chemical composition and manufacture

Definitions

  • This invention relates to a process for obtaining electrodeposited rhodium layers which have a low stress and to the bath for obtaining such low stress deposits.
  • Among other objects of the invention is to provide a body having a rhodium deposit under low internal stress.
  • Among other objects of the invention is to provide a process of plating rhodium under low stress.
  • the objects of the present invention are obtained by providing a rhodium sulfate-sulfuric acid bath and add ing to this bath to 100 g./l. of magnesium sulfate (MgSO).
  • MgSO magnesium sulfate
  • the cathode efliciency of a rhodium sulfate sulfuric acid bath may be as high as about 88-90%.
  • the efficiency remains high.
  • the deposits show a tendency to curl toward the base indicating that the rhodium deposit is under compressive stress.
  • the free sulfuric acid content of the bath is from 20 to 100 cc./l. Very satisfactory results are obtained with 50 cc. of free sulfuric acid per liter.
  • the rhodium sulfate content of the bath is such as to provide about 2 g. to 5g. of rhodium per liter. Higher amounts of rhodium may be employed but with such higher amounts drag-out and other losses are increased without increasing the efliciency.
  • the bath may be operated from room temperature (approximately 20 C.) to about 50 C. and at crnrent densities of from 4 to 20 amperes per square foot of cathode. The higher current densities produce slightly more stress. Plating at about 10 amperes per square foot and 50 C. with mild agitation yields a good deposit at about cathode efliciency.
  • a convenient qualitative test to determine stress in the deposit is to dissolve away the basis metal from a rhodium deposited body with nitric acid for example. If the basis metal is dissolved from an article having a rhodium film deposited from the common complex rhodium phosphate bath the rhodium disintegrates into small flakes. This indicates that the deposit has high internal stress.
  • Example 1 A sheet of metal, for example brass, is made the cathode in an electroplating bath comprising 5 g./l. of rhodium (as rhodium sulfate) 50 cc./l. of sulfuric acid, and 50 g./l. of magnesium sulfate.
  • the bath is maintained at 50 C. and operated at a current density of approximately 10 amperes per square foot until a thickness of about 0.0003" is obtained.
  • the deposit has a slight grey appearance but is smooth.
  • the efiiciency of the bath is 85%. Spectrographic examination of the plated article did not indicate the presence of any magnesium.
  • the basis metal could be dissolved away from this prodnet to leave a thin continuous film of rhodium.
  • a process of electroplating rhodium metal under low internal stress comprising electrodepositing rhodium upon a basis metal from an aqueous bath consisting essentially of 20-100 cc. per liter of free sulfuric acid, 2 to about 5 grams per liter of rhodium added as rhodium sulfate and 10-100 grams per liter of magnesium sulfate, the remainder being water, electrodepositing rhodium from said bath at a current density of from 4 to 20 amperes per square foot and at a temperature of about 20 C. to about 50 C.
  • An electroplating bath for depositing rhodium therefrom comprising an aqueous bath consisting essentially of 20-100 cc. per liter of free sulfuric acid, 2 to 5 grams per liter of rhodium added as rhodium sulfate, 20-100 grams per liter of magnesium sulfate and the remainder being water.
  • An electroplated article comprising a basis metal and a substantially stress-free electrodeposited layer of rhodium thereon, said article having been prepared by the process of claim 1.

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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)
  • Electroplating And Plating Baths Therefor (AREA)

Description

atent 2,895,889: Patented July 21, 1959 LOW STRESS ELECTKODEPOSITED RHODIUIVI Karl Schurnpelt, Union, N .J assignor to Sal-Rex Precious lIVIetals, Inc., Belleville, N.J., a corporation of New ersey No Drawing. Application January 10, 1957 Serial No. 633,381
Claims. (Cl. 204-47) This invention relates to a process for obtaining electrodeposited rhodium layers which have a low stress and to the bath for obtaining such low stress deposits.
Internal stress in metallic deposits causes the deposit to crack, peel or distort. Shrinkage in a highly stressed deposit may cause premature fatigue failure of the basis metal. Where it is known that a metal deposit is likely to be plated under stress a severe etching of the basis metal before plating is usually essential in order to obtain a satisfactory product. It is desirable, therefore, to be able to plate a metal such as rhodium under low stress but little is known as to the exact cause of internal stress in electrodeposited metals.
Among the objects of this invention is to provide an electroplating composition capable of plating rhodium metal under low stress.
Among other objects of the invention is to provide a body having a rhodium deposit under low internal stress.
Among other objects of the invention is to provide a process of plating rhodium under low stress.
A fairly comprehensive study of rhodium plating was made by Wiesner and reported in 39th Annual Proceedings and Technical Sessions, American Electroplaters Society (published in 1952), pp. 79-99. According to this article the addition of a small amount of chloride ion to a rhodium electroplating bath (which may be the rhodium sulfate or the complex rhodium phosphate bath) reduces the stress of the deposit. The chloride ion also causes a reduction in brightness. If the chloride ion exceeds a certain minimum amount of about 0.3 g./l. the deposit obtained is rough. Wiesner also found that operating the baths at higher temperatures (3854 C., for example) reduced the stress in the deposit. Common organic addition agents such as saccharine employed for reducing stress of deposits from nickel baths were found to reduce the cathode efliciency a prohibitive amount.
The objects of the present invention are obtained by providing a rhodium sulfate-sulfuric acid bath and add ing to this bath to 100 g./l. of magnesium sulfate (MgSO The cathode efliciency of a rhodium sulfate sulfuric acid bath may be as high as about 88-90%. After the addition of magnesium sulfate the efficiency remains high. Instead of having an internal tensile stress tending to pull the rhodium film away from the basis metal the deposits show a tendency to curl toward the base indicating that the rhodium deposit is under compressive stress.
The free sulfuric acid content of the bath is from 20 to 100 cc./l. Very satisfactory results are obtained with 50 cc. of free sulfuric acid per liter.
The rhodium sulfate content of the bath is such as to provide about 2 g. to 5g. of rhodium per liter. Higher amounts of rhodium may be employed but with such higher amounts drag-out and other losses are increased without increasing the efliciency.
The bath may be operated from room temperature (approximately 20 C.) to about 50 C. and at crnrent densities of from 4 to 20 amperes per square foot of cathode. The higher current densities produce slightly more stress. Plating at about 10 amperes per square foot and 50 C. with mild agitation yields a good deposit at about cathode efliciency.
A convenient qualitative test to determine stress in the deposit is to dissolve away the basis metal from a rhodium deposited body with nitric acid for example. If the basis metal is dissolved from an article having a rhodium film deposited from the common complex rhodium phosphate bath the rhodium disintegrates into small flakes. This indicates that the deposit has high internal stress.
The following examples further illustrate the principals and operation of the invention.
Example 1 A sheet of metal, for example brass, is made the cathode in an electroplating bath comprising 5 g./l. of rhodium (as rhodium sulfate) 50 cc./l. of sulfuric acid, and 50 g./l. of magnesium sulfate. The bath is maintained at 50 C. and operated at a current density of approximately 10 amperes per square foot until a thickness of about 0.0003" is obtained. The deposit has a slight grey appearance but is smooth. The efiiciency of the bath is 85%. Spectrographic examination of the plated article did not indicate the presence of any magnesium. The basis metal could be dissolved away from this prodnet to leave a thin continuous film of rhodium.
The features and principles underlying the invention described above in connection with specific exemplifications will suggest to those skilled in the art many other modifications thereof. It is accordingly desired that the appended claims shall not be limited to any specific feature or details thereof.
I claim:
1. A process of electroplating rhodium metal under low internal stress comprising electrodepositing rhodium upon a basis metal from an aqueous bath consisting essentially of 20-100 cc. per liter of free sulfuric acid, 2 to about 5 grams per liter of rhodium added as rhodium sulfate and 10-100 grams per liter of magnesium sulfate, the remainder being water, electrodepositing rhodium from said bath at a current density of from 4 to 20 amperes per square foot and at a temperature of about 20 C. to about 50 C.
2. The process as set forth in claim 1 wherein said bath contains 50 cc. per liter of sulfuric acid and 50 grams per liter of magnesium sulfate.
3. An electroplating bath for depositing rhodium therefrom comprising an aqueous bath consisting essentially of 20-100 cc. per liter of free sulfuric acid, 2 to 5 grams per liter of rhodium added as rhodium sulfate, 20-100 grams per liter of magnesium sulfate and the remainder being water.
4. The bath as claimed in claim 3 containing 50 cc. per liter of sulfuric acid and 50 grams per liter of magnesium sulfate.
5. An electroplated article comprising a basis metal and a substantially stress-free electrodeposited layer of rhodium thereon, said article having been prepared by the process of claim 1.
References Cited in the file of this patent UNITED STATES PATENTS Shields Feb. 27, 1934 OTHER REFERENCES

Claims (1)

1. A PROCESS OF ELECRROPLATING RHODIUM METAL UNDER LOW INTERNAL STRESS COMPRISING ELECTRODEPOSITING RHODIUM UPON A BASIS METAL FROM AN AQUEOUS BATH CONSISTING ES-SENTIALLY OF 20-100 CC. PER LITER OF FREE SULFURIC ACID, 2 TO ABOUT 5 GRAMS PERLITER OF RHODIUM ADDED AS RHODIUM SULFATE AND 10-100 GRAMS PER LITER OF MAGNESIUM SULFATE, THE REMAINDER BEING WATER, ELECTRODEPOSITING RHODIUM FROM SAID BATH AT A CURRENT DENSITY OF FROM 4 TO 20 AMPERES PER SQUARE FOOT AND AT A TEMPERATURE OF ABOUT 20* C. TO ABOUT 50* C.
US633381A 1957-01-10 1957-01-10 Low stress electrodeposited rhodium Expired - Lifetime US2895889A (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
DENDAT1068081D DE1068081B (en) 1957-01-10
NL111673D NL111673C (en) 1957-01-10
DENDAT1072047D DE1072047B (en) 1957-01-10 068 OSl)
US633381A US2895889A (en) 1957-01-10 1957-01-10 Low stress electrodeposited rhodium
US663595A US2895890A (en) 1957-01-10 1957-06-05 Low stress electrodeposited rhodium
GB31318/57A GB836475A (en) 1957-01-10 1957-10-07 Low stress electrodeposited rhodium
GB38673/57A GB835830A (en) 1957-01-10 1957-12-12 Low stress electrodeposited rhodium
CH5393857A CH378635A (en) 1957-01-10 1957-12-18 Process for electrodeposition of rhodium metal
FR1189477D FR1189477A (en) 1957-01-10 1958-01-03 Electrolytically deposited low internal voltage rhodium
FR759094A FR72983E (en) 1957-01-10 1958-02-25 Electrolytically deposited low internal voltage rhodium
CH5685658A CH418084A (en) 1957-01-10 1958-03-10 Process for electrodeposition of rhodium metal

Applications Claiming Priority (1)

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US633381A US2895889A (en) 1957-01-10 1957-01-10 Low stress electrodeposited rhodium

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3891741A (en) * 1972-11-24 1975-06-24 Ppg Industries Inc Recovery of fission products from acidic waste solutions thereof
US3922231A (en) * 1972-11-24 1975-11-25 Ppg Industries Inc Process for the recovery of fission products from waste solutions utilizing controlled cathodic potential electrolysis
US4330376A (en) * 1979-03-05 1982-05-18 Atlantic Richfield Company Process for inhibiting titanium corrosion
US4789437A (en) * 1986-07-11 1988-12-06 University Of Hong Kong Pulse electroplating process
US20070012575A1 (en) * 2005-07-12 2007-01-18 Morrissey Ronald J Bright rhodium electrodeposition

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1949131A (en) * 1932-11-14 1934-02-27 Thomas P Shields Rhodium plating

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1949131A (en) * 1932-11-14 1934-02-27 Thomas P Shields Rhodium plating

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3891741A (en) * 1972-11-24 1975-06-24 Ppg Industries Inc Recovery of fission products from acidic waste solutions thereof
US3922231A (en) * 1972-11-24 1975-11-25 Ppg Industries Inc Process for the recovery of fission products from waste solutions utilizing controlled cathodic potential electrolysis
US4330376A (en) * 1979-03-05 1982-05-18 Atlantic Richfield Company Process for inhibiting titanium corrosion
US4789437A (en) * 1986-07-11 1988-12-06 University Of Hong Kong Pulse electroplating process
US20070012575A1 (en) * 2005-07-12 2007-01-18 Morrissey Ronald J Bright rhodium electrodeposition

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Owner name: HOOKER CHEMICALS & PLASTICS CORP.

Free format text: MERGER;ASSIGNOR:OXY METAL INDUSTRIES CORPORATION;REEL/FRAME:004075/0885

Effective date: 19801222

AS Assignment

Owner name: OCCIDENTAL CHEMICAL CORPORATION

Free format text: CHANGE OF NAME;ASSIGNOR:HOOKER CHEMICAS & PLASTICS CORP.;REEL/FRAME:004126/0054

Effective date: 19820330