US3037918A - Semi-bright copper - Google Patents

Semi-bright copper Download PDF

Info

Publication number
US3037918A
US3037918A US42755A US4275560A US3037918A US 3037918 A US3037918 A US 3037918A US 42755 A US42755 A US 42755A US 4275560 A US4275560 A US 4275560A US 3037918 A US3037918 A US 3037918A
Authority
US
United States
Prior art keywords
baths
leveling
bath
copper
semi
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
US42755A
Inventor
Barnet D Ostrow
Fred I Nobel
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 US42755A priority Critical patent/US3037918A/en
Application granted granted Critical
Publication of US3037918A publication Critical patent/US3037918A/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
    • C25D3/38Electroplating: Baths therefor from solutions of copper
    • C25D3/40Electroplating: Baths therefor from solutions of copper from cyanide baths, e.g. with Cu+

Definitions

  • the present invention is directed to alkaline cyanide copper plating baths and more particularly to semi-bright baths having a leveling or smoothing eifect to reduce surface micro-roughness.
  • the prior art cyanide copper baths even with addition agents were unable to reduce surface roughness or hide imperfections on comparatively smooth surfaces (R.M.S. values of 10 or below) unless periodic reverse current was used.
  • the baths described in this invention are capable of producing positive leveling in cyanide copper baths without the use of periodic reverse current on surfaces that had initial roughness of approximately 10 R.M.S. or less. If periodic reverse current is utilized with the baths of this invention, then the degree of leveling becomes considerably enhanced, in fact far better than that secured from prior art periodic reverse cyanide copper baths.
  • the present invention is intended and adapted to overcome the deficiencies and disadvantgaes inherent in cyanide copper plating baths, it being among the objects thereof to introduce into such baths an addition agent which will have a leveling effect on a copper deposit without using periodic reverse current, to eliminate surface roughness of about 10-15 R.M.S. and lower.
  • R is a hydrocarbon radical having 2 to 3 carbon atoms
  • X is hydrogen or [OR] OH
  • n is 0 to 20.
  • the leveling efiect of the above class of compounds is enhanced by the presence of a small amount of zinc in the soluble form, such as sodium zincate or zinc cyanide.
  • a small amount of zinc in the soluble form such as sodium zincate or zinc cyanide.
  • concentration of the zinc in the range of 0.01 to 1.0 g./l. gives excellent results.
  • the optimum range is between 0.1 and 0.2 g./l.
  • the bath In order to obtain good leveling it is important that the bath contain a limited concentration of the selenium, tellurium, or sulfur type brighteners.
  • Selenium having a valence of -2, sulfur in the sulfide state and tellurium should not be present in amounts exceeding 0.0005 g./l.
  • controlled amounts of selenium (in the -2 state) or sulfidic sulfur may be utilized within the above limits, say from 0.0001 to 0.0005 g./l. whereby increased brightness of deposit is obtained without impairing appreciably the micro-leveling characteristic of the bath.
  • the Plating is conducted at temperatures of 7 1 5.
  • a plating bath according to claim 1 characterized in F. with a current density of 10 to 40 amperes per square foot. Mild to vigorous agitation is provided.
  • those of larger molecular weight or of more complex structure are preferred'.
  • those hydroxy polyamines which have ether linkages have a greater leveling efiect than those which do not contain such ether linkages. Mixtures of hydroxy 'polyamines are more effective than single compounds.
  • the present cyanide baths exhibit micro-leveling whereas the acid copper baths exhibit macro-leveling. However, it is possible to obtain microas well as macroleveling from these cyanide baths by utilizing periodic reverse current.
  • R represents a hydrocarbon radical having from 2 to 3 carbon atoms
  • X represents hydrogen and -[OR] -OH
  • n is 0 to 20, the amount of said compound present in the bath being sufiicient to produce micro-leveling in the deposit.
  • a plating bath according to claim 1 characterized in that the amount of said compound is about 0.1 to 50.0 g./l.
  • a plating bath according to claim 1 characterized in that said bath contains less than 1.0 g./l. of a soluble zinc salt.
  • a plating bath according to claim 1 characterized in that said bath contains about 0.01 to 1.0 g./l. of a soluble zinc salt.
  • said bath is substantially free from soluble compounds of selenium, tellurium and sulfur.
  • a plating bath according to claim 1 characterized in that said bath contains not over 0.0005 g./l. of soluble compounds of selenium, tellurium and sulfur.
  • a plating bath according to claim 1 characterized in that saidcompound has from 1 to 4 free OH groups.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (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

United States Patent No Drawing. Filed .iuly 14, 1960, Ser. No. 42,755 8 Claims. (Cl. 204-52) The present invention is directed to alkaline cyanide copper plating baths and more particularly to semi-bright baths having a leveling or smoothing eifect to reduce surface micro-roughness.
In certain applications of copper deposits it is more desirable to obtain leveling than to obtain a high degree of brightness. Of the bright cyanide copper baths in the prior art, none had the ability of depositing coatings which would hide or level surface imperfections on the basis metal without using periodic reverse currents. Actually, such prior baths often exerted a negative leveling; i.e., they magnified the imperfections. The prior art addition agents further tended to accentuate the negative leveling effect of the bath. It is known that the prior art acid copper plating baths can be made to level or reduce surface roughness of the basis metal when certain organic addition agents are incorporated in the bath. For instance, such acid baths are capable of reducing the surface roughness of a comparatively rough surface to R.M.S. value of about 30.
On the other hand, the prior art cyanide copper baths even with addition agents were unable to reduce surface roughness or hide imperfections on comparatively smooth surfaces (R.M.S. values of 10 or below) unless periodic reverse current was used. The baths described in this invention are capable of producing positive leveling in cyanide copper baths without the use of periodic reverse current on surfaces that had initial roughness of approximately 10 R.M.S. or less. If periodic reverse current is utilized with the baths of this invention, then the degree of leveling becomes considerably enhanced, in fact far better than that secured from prior art periodic reverse cyanide copper baths.
The present invention is intended and adapted to overcome the deficiencies and disadvantgaes inherent in cyanide copper plating baths, it being among the objects thereof to introduce into such baths an addition agent which will have a leveling effect on a copper deposit without using periodic reverse current, to eliminate surface roughness of about 10-15 R.M.S. and lower.
It is also among the objects of the invention to provide a bath of the character described which is adapted to produce a crystal structure of the deposited copper which, while only semi-bright, can be readily brightened by the subsequent bright nickel coatings.
It is further among the objects of the invention to provide a bath of such character that even if the copper deposit is burned, the subsequent nickel coating tends to brighten readily.
' ing or leveling eifect and brighten the deposit. The bright- It is still further among the objects of the invention to provide a cyanide copper bath that will produce leveling with or without reverse current from the same bath.
In practicing the present invention there is provided the usual cyanide copper plating baths, for instance:
G./l. CuCN 45-75 Total KCN 75-120 KOH 15-30 ness approximates that obtained by the practice of US. Patent No. 2,287,654, describing the use of ,thiocyanate in the bath, which has no leveling elfect without periodic reverse current. Actually in such prior baths, selenium or sulfur in the 2 state and tellurium in the 2 and +4 state, destroy leveling when present in concentrations required or recommended to give full or maximum brightness of the deposit.
The compounds which are the addition agents of the present invention are of the type set forth in Table I below:
The compounds of the present invention may be included in the following general formula:
wherein R is a hydrocarbon radical having 2 to 3 carbon atoms, X is hydrogen or [OR] OH and n is 0 to 20.
The leveling efiect of the above class of compounds is enhanced by the presence of a small amount of zinc in the soluble form, such as sodium zincate or zinc cyanide. In high efliciency cyanide copper baths the concentration of the zinc in the range of 0.01 to 1.0 g./l. gives excellent results. The optimum range is between 0.1 and 0.2 g./l.
In order to obtain good leveling it is important that the bath contain a limited concentration of the selenium, tellurium, or sulfur type brighteners. Selenium having a valence of -2, sulfur in the sulfide state and tellurium should not be present in amounts exceeding 0.0005 g./l. However, controlled amounts of selenium (in the -2 state) or sulfidic sulfur may be utilized within the above limits, say from 0.0001 to 0.0005 g./l. whereby increased brightness of deposit is obtained without impairing appreciably the micro-leveling characteristic of the bath.
Table II attached hereto contains a number of specific examples which will illustrate the nature of the invention.
ROX
ROX
Table 11 CuCN .l- 60 75 45 75 60 75 6O 60 i 94 KOH 15 20 15 30 30 15 15 15' Znaszineateor Cyanie 0.2 0.3 0.15 0.2 0.5 0.4
The Plating is conducted at temperatures of 7 1 5. A plating bath according to claim 1 characterized in F. with a current density of 10 to 40 amperes per square foot. Mild to vigorous agitation is provided.
Among the present addition agents, those of larger molecular weight or of more complex structure are preferred'. Those hydroxy polyamines which have ether linkages have a greater leveling efiect than those which do not contain such ether linkages. Mixtures of hydroxy 'polyamines are more effective than single compounds.
While the amounts used may vary from 0.01 to 50.0 g./l., it is preferred to employ from 0.5 to 10.0 g./l, in most applications.
The present cyanide baths exhibit micro-leveling whereas the acid copper baths exhibit macro-leveling. However, it is possible to obtain microas well as macroleveling from these cyanide baths by utilizing periodic reverse current.
' We claim: 7
1. An aqueous alkaline cyanide copper plating bath having incorporated therein a compound having the following formula:
/R 0 X -RN X-O R BOX wherein R represents a hydrocarbon radical having from 2 to 3 carbon atoms, X represents hydrogen and -[OR] -OH, and n is 0 to 20, the amount of said compound present in the bath being sufiicient to produce micro-leveling in the deposit.
2. A plating bath according to claim 1 characterized in that the amount of said compound is about 0.1 to 50.0 g./l.
3. A plating bath according to claim 1 characterized in that said bath contains less than 1.0 g./l. of a soluble zinc salt.
4. A plating bath according to claim 1 characterized in that said bath contains about 0.01 to 1.0 g./l. of a soluble zinc salt.
that said bath is substantially free from soluble compounds of selenium, tellurium and sulfur.
' 6. A plating bath according to claim 1 characterized in that said bath contains not over 0.0005 g./l. of soluble compounds of selenium, tellurium and sulfur.
"I. A plating bath according to claim 1 characterized in that saidcompound has from 1 to 4 free OH groups.
and at least one ether group.
' References Cited in the file of this patent UNITED STATES PATENTS Portzer Nov. 26, 1957 Winters May 6, 1958

Claims (1)

1. AN AQUEOUS ALKALINE CYANIDE COPPER PLATING BATH HAVING INCORPORATED THEREIN A COMPOUND HAVING THE FOLLOWING FORMULA:
US42755A 1960-07-14 1960-07-14 Semi-bright copper Expired - Lifetime US3037918A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US42755A US3037918A (en) 1960-07-14 1960-07-14 Semi-bright copper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US42755A US3037918A (en) 1960-07-14 1960-07-14 Semi-bright copper

Publications (1)

Publication Number Publication Date
US3037918A true US3037918A (en) 1962-06-05

Family

ID=21923580

Family Applications (1)

Application Number Title Priority Date Filing Date
US42755A Expired - Lifetime US3037918A (en) 1960-07-14 1960-07-14 Semi-bright copper

Country Status (1)

Country Link
US (1) US3037918A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3276977A (en) * 1962-02-13 1966-10-04 Dehydag Deutsche Hvdrierwerke Metal electroplating process and bath
US4376685A (en) * 1981-06-24 1983-03-15 M&T Chemicals Inc. Acid copper electroplating baths containing brightening and leveling additives

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2814590A (en) * 1954-07-20 1957-11-26 Lloyd B Portzer Electrodeposition of copper
US2833705A (en) * 1956-12-14 1958-05-06 John B Winters Cadmium plating

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2814590A (en) * 1954-07-20 1957-11-26 Lloyd B Portzer Electrodeposition of copper
US2833705A (en) * 1956-12-14 1958-05-06 John B Winters Cadmium plating

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3276977A (en) * 1962-02-13 1966-10-04 Dehydag Deutsche Hvdrierwerke Metal electroplating process and bath
US4376685A (en) * 1981-06-24 1983-03-15 M&T Chemicals Inc. Acid copper electroplating baths containing brightening and leveling additives

Similar Documents

Publication Publication Date Title
US2171842A (en) Electroplating
US3966564A (en) Method of electrodepositing an alloy of tin, cobalt and a third metal and electrolyte therefor
EP0196053A2 (en) Chromium plating process for producing non-iridescent, adherent, bright chromium deposits at high efficiencies and substantially free of cathodic low current density etching
US3666640A (en) Gold plating bath and process
GB2093861A (en) Bath for electrodeposition of chromium
US2732336A (en) Electroplating composition for copper
US5006208A (en) Galvanic gold alloying bath
US4184929A (en) Trivalent chromium plating bath composition and process
US3037918A (en) Semi-bright copper
US2770587A (en) Bath for plating bright copper
US3881919A (en) Ternary alloys
US2402185A (en) Tin electrodepositing composition and process
US2113517A (en) Electrodeposition of silver
US2383798A (en) Electroplating
US2181773A (en) Brass plating
US2380044A (en) Process for producing electrodeposits
US2080479A (en) Plating of zinc
US2989448A (en) Brass, copper-tin, and copper plating bath brightener
US2497988A (en) Indium plating
US2427280A (en) Nickel electroplating composition
US2541700A (en) Electroplating copper
US2854389A (en) Bright copper plating process
US2080483A (en) Electrodeposition of zinc
US2694041A (en) Electrodeposition of nickel
US3092559A (en) Gold plating