US3174918A - Bright gold electroplating - Google Patents

Bright gold electroplating Download PDF

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Publication number
US3174918A
US3174918A US84517A US8451761A US3174918A US 3174918 A US3174918 A US 3174918A US 84517 A US84517 A US 84517A US 8451761 A US8451761 A US 8451761A US 3174918 A US3174918 A US 3174918A
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Prior art keywords
silver
gold
bright
deposits
bath
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US84517A
Inventor
Rinker Edwin Cornell
Foulke Donald Gardner
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Occidental Chemical Corp
Sel Rex Corp
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Sel Rex Corp
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Publication date
Priority to NL273924D priority Critical patent/NL273924A/xx
Priority to CH51162A priority patent/CH399865A/en
Application filed by Sel Rex Corp filed Critical Sel Rex Corp
Priority to US84517A priority patent/US3174918A/en
Priority to GB45060/61A priority patent/GB939007A/en
Priority to FR885252A priority patent/FR1311023A/en
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Publication of US3174918A publication Critical patent/US3174918A/en
Assigned to OXY METAL INDUSTRIES CORPORATION reassignment OXY METAL INDUSTRIES CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). 4-09-74 Assignors: OXY METAL FINISHING CORPORATION
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
    • C25D3/56Electroplating: Baths therefor from solutions of alloys
    • C25D3/62Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of gold

Definitions

  • This invention is based on the discovery that silver acts as a brightener, in what are essentially non-cyanide baths providing the silver ion concentration is maintained small by adding complexing or chelating agents to the bath, for example. Under these circumstances, the bath pH may be maintained over relatively wide pH values; 6 to 13 in contrast to the normal bright gold plating baths employing silver as an addition agent where the pH values in practice have been of the order of 12.
  • the baths of the present invention may be operated at a pH of 6l3, there is a definite advantage in being able to operate a bright gold bath at a pH of 6.5 to 7.0, with a low content of free cyanide, especially when plating workpieces such as printed circuit boards where the solvent action of the alkaline cyanide bath on the copper-plastic laminate is a problem.
  • This invention provides a bath which has relatively low susceptibility to the effect or".
  • foreign ions such as nickel, copper and other base metal ions, which ions normally have a deleterious effect on brightness effected by the silver ion by virtue of the presence of the silver complexing agent which in general will complex higher valent cations more effectively.
  • the objects of the invention are attained by providing an aqueous bath containing about 4-20 g./l. of potas sium gold cyanide, 25-300 mg./l. of silver ion and 5400 g./l. of one or more alkali metal salts. To this hath no free cyanide is added although a limited amount of free cyanide may be set free as the bath is operated.
  • alkali metal gold cyanide provides the necessary gold ions for the orderly disposition of the gold, but does not supply sufiicient ions to provide the conductivity required for good commercial operation of the bath. Consequently, alkali metal such as sodium or, preferably potassium salts of organic acids, inorganic and organo-inorganic acids, (re added to provide the nectill essary conductivity.
  • alkali metal sulfates, phosphates, nitrates, sulfamates, and the alkali metal salts of such organic acids as citrate, tartrate, lactate, as well as the organo-inorganic acid such as naphthalene sulfonic, benzene sulfonic acids are useful in this connection.
  • the bath contains the following ingredients:
  • Alkali hydroxide Suflicient to produce pH of 6.5l3 preferably pH 6.57.5.
  • Chelating agent l to 50 g./l.
  • the chelating or complexing agent for silver must be such that the silver ion concentration, with 5 to 50 grams per liter of the agent present, will be reduced to no more than that provided by potassium or sodium silver cyanide in the presence of free potassium cyanide. Otherwise, the silver salt must be kept at low concentration and fed frequently. If silver is added as potassium silver cyanide, as silver-sulfate, nitrate or other soluble silver salt, the available silver ions in the cathode film are considerable with the result that rapid deposition of silver along with the gold occurs.
  • minor brightening agents such as potassium nickel and cobalt cyanides may be added to the aforedescribed bath to provide a small increase in brilliance, but in general, these materials are unnecessary and contribute to deposit brittleness.
  • Example 1 In an amount of water sufficient to provide one liter of solution was dissolved:
  • Example 2 in an amount of Water sufiicient to provide one liter of solution was added:
  • Example 4 In an amount of water sufficient to provide one liter of solution was added:
  • Example 5 In an amount of water sufiicient to provide one liter of solution was added:
  • Triglycollamic acid gm Triglycollamic acid gm.
  • Example 6 To the bath of Example 5, absent the silver nitrate, was added 145 mg./l. of silver sulfate. Again not all the silver salt dissolved at once, but a bright deposit was obtained.
  • Silver salts silver fluoride, silver acetate.
  • the above baths were normally operated at room temperature, but they can be operated up to a temperature of 45 C. Above this temperature hazy deposits are apt to be obtained.
  • the baths can be operated at temperatures down to about 15 C.
  • the normal current density range is 1 to 5 a.s.f. (0.1O.5 amp/43m?) depending upon the gold content, the temperature, and the rate of agitation. At higher temperatures, high gold content and very vigorous agitation, considerably higher current densities can be employed, but the control of commercial baths becomes somewhat more critical.
  • agitation either solution volume or mechanical agitation is useful and, actually air agitation is etleetive for this bath in contrast to high free cyanide gold baths where the ethciency drops rapidly when air agitation is used.
  • An aqueous electrolyte for the production of bright gold deposits consisting essentially of the following ingredients:
  • KAu(CN) (calculated as Au) 4 to 20 g./l.
  • KAg(CN) (calculated as Ag) 25 to 500 mg./l.
  • Alkali metal conducting salt (other than cyanide) 5 to g./l.
  • Alkali hydroxide to pH 6.513.
  • Triglycollamic acid 5 to 10 g./l.
  • An aqueous electrolyte for the production of bright gold deposits consisting essentially of the following ingredients:

Description

dillfild Patented Mar. 23, 1965 3,174,918 BRIGHT QQLD ELECTRQPLATING Edwin Cornell Thinker, Morristown, and Donald Gardner l 'oulke, Watchnng, Plainlield, Nah, assignors to Sol-Rex (Jorporation, Nutiey, NJ., a corporation of New .l'ersey No Drawing. Filed lien. 24, $61, Ser. No. 34,517 2 Claims. (Cl. 294- 43) This invention relates to the electrodeposition of gold to obtain bright gold deposits and to the electrolytes for obtaining such deposits.
Among the objects of the invention are to provide a gold plating bath and process which will produce bright gold deposits.
In the past, it has been possible to obtain bright gold deposits from gold cyanide baths, particularly in the case of baths rather high in free cyanide, by the addition of silver ions as a brightening agent. The effectiveness of the silver ion as a brightener appears to be related to the complexing ability of the cyanide ion on the silver whereby a limited amount of silver is free to join the gold atoms in the crystal lattice.
This invention is based on the discovery that silver acts as a brightener, in what are essentially non-cyanide baths providing the silver ion concentration is maintained small by adding complexing or chelating agents to the bath, for example. Under these circumstances, the bath pH may be maintained over relatively wide pH values; 6 to 13 in contrast to the normal bright gold plating baths employing silver as an addition agent where the pH values in practice have been of the order of 12.
Although the baths of the present invention may be operated at a pH of 6l3, there is a definite advantage in being able to operate a bright gold bath at a pH of 6.5 to 7.0, with a low content of free cyanide, especially when plating workpieces such as printed circuit boards where the solvent action of the alkaline cyanide bath on the copper-plastic laminate is a problem.
There is a definite advantage in being able to operate a gold plating bath in the lower portion of the pH range of 6 to 13, for example, at a pH of 6.5 to 7 or even up to 9 or 10. Thus, such, baths having little or substantially no free cyanide or alkali content do not deleteriously effect the copper-plastic laminate of printed circuit boards which are immersed therein for plating.
Among other objects of the invention, therefore, is to provide a process and electrolyte capable of plating bright gold deposits without the presence of any substantial amount of alkali or alkali cyanides.
This invention provides a bath which has relatively low susceptibility to the effect or". foreign ions such as nickel, copper and other base metal ions, which ions normally have a deleterious effect on brightness effected by the silver ion by virtue of the presence of the silver complexing agent which in general will complex higher valent cations more effectively.
Among other objects of the invention, therefore, is to provide a bright gold plating solution containing silver ions which has a low susceptibility to foreign ions.
The objects of the invention are attained by providing an aqueous bath containing about 4-20 g./l. of potas sium gold cyanide, 25-300 mg./l. of silver ion and 5400 g./l. of one or more alkali metal salts. To this hath no free cyanide is added although a limited amount of free cyanide may be set free as the bath is operated.
The alkali metal gold cyanide provides the necessary gold ions for the orderly disposition of the gold, but does not supply sufiicient ions to provide the conductivity required for good commercial operation of the bath. Consequently, alkali metal such as sodium or, preferably potassium salts of organic acids, inorganic and organo-inorganic acids, (re added to provide the nectill essary conductivity. We have found that the alkali metal sulfates, phosphates, nitrates, sulfamates, and the alkali metal salts of such organic acids as citrate, tartrate, lactate, as well as the organo-inorganic acid such as naphthalene sulfonic, benzene sulfonic acids are useful in this connection.
Thus, the bath contains the following ingredients:
l Au(CN) (calculated as Au) 4 to 20 g./l. KAg(CN) (calculated as Ag) 25 to 500 m./l.
Conducting salt 5 to g./l.
Alkali hydroxide Suflicient to produce pH of 6.5l3 preferably pH=6.57.5.
lQNilICN), or K CMCNL,
(optional) Up to 15 g./l.
Chelating agent l to 50 g./l.
The chelating or complexing agent for silver must be such that the silver ion concentration, with 5 to 50 grams per liter of the agent present, will be reduced to no more than that provided by potassium or sodium silver cyanide in the presence of free potassium cyanide. Otherwise, the silver salt must be kept at low concentration and fed frequently. If silver is added as potassium silver cyanide, as silver-sulfate, nitrate or other soluble silver salt, the available silver ions in the cathode film are considerable with the result that rapid deposition of silver along with the gold occurs. This results in a large concentration gradient in the diffusion layer at the cathode and the concomitant rapid supply of silver ions to the cathode which, of course, makes for rapid silver deposition on a continuing basis unless the silver salt concentration is very low. Under such conditions, the gold deposit assumes a brownish, greenish, unattractive appearance. However, the addition of chelating or complexing compounds such as the salts of triglycollamic acid, ethylenediamine tetraacetic acid (EDTA), and amines which complex the silver ion so that supply to the cathode surface is sufiicient to provide just enough silver ions to provide a gold deposit which is bright over wide current density ranges.
Other minor brightening agents, such as potassium nickel and cobalt cyanides may be added to the aforedescribed bath to provide a small increase in brilliance, but in general, these materials are unnecessary and contribute to deposit brittleness.
The practice of this invention can best be described by citing a number of examples of baths which have been found to provide excellent bright gold deposits. In all these examples, a bright gold deposit of a thickness of more than 10 millionths of an inch was obtained. Thus, the term bright gold deposit will be understood to mean deposits which are substantially thicker than flash deposits.
Example 1 In an amount of water sufficient to provide one liter of solution was dissolved:
Silver (as KAg(Ci l) mg K PO gm 6 g[].'l 2 Gold (as KAu(CN) gm 8 The deposit upon a polished brass panel 3 /2" 7; 1" was very bright at 2 a.s.f. and 4 a.s.f. (3 and 3.9 volts), at a pH of 11.0. The efficiency Was 100 mg./ampereminute.
Example 2 in an amount of Water sufiicient to provide one liter of solution was added:
Triglycollamic acid 10 gm.
KOH To pH of 11.0. Gold (as l IAu(CN) 8 gm.
Silver (as l Ag(CN) 100 mg.
In an amount of water sufiicient to provide one liter of solution was added:
Disodium EDTA 10 gm. KOH To pH of 10.
Gold (as KAu(CN) 8 gm.
Silver (as KAg(CN) 1 mg.
Excellent bright deposits were obtained at a current density of 3 and 4 a.s.f.
Example 4 In an amount of water sufficient to provide one liter of solution was added:
Triglycollamic acid 10* gm.
Naphthalene sulfonic acid, Na salt 10 gm.
KOH To pH of 8.
Gold (as KAu(CN) 8 gm.
Silver (as KAg(CN) 100 mg.
Example 5 In an amount of water sufiicient to provide one liter of solution was added:
Triglycollamic acid gm.
Potassium hydroxide To adjust pH of 6.5. Silver nitrate 155 mg.
Gold (as KAu(CN) 8 gm.
Even though all the silver nitrate did not dissolve at once, bright deposits were obtained.
Example 6 To the bath of Example 5, absent the silver nitrate, was added 145 mg./l. of silver sulfate. Again not all the silver salt dissolved at once, but a bright deposit was obtained.
Example 7 To a liter of water were added:
Disodium EDTA g1 l0 KH PO gm 5 Gold (as KAu(CN) gm 8 Silver (as KAg(CN) mg 200 pH 7.0
Bright deposits were obtained at 3 a.s.f.
Example 8 To a liter of water were added:
Potassium dihydrogen phosphate gm 10 Diethylethanolamine gm 5 Gold (as KAu(CN) gm 8 Silver (as KAg(CN) mg 100 pH 7.0
Bright deposits were obtained at 3 a.s.f.
Example 9 To a liter of water were added:
Sodium citrate gm 10 KAI1(CN) gm 11 KAg(CN) mg 200 pH 10.5
Bright deposits were obtained from this bath at 4 a.s.f.,
4 and when 10 g./l. o1"- K NKCNM were added, the deposit was brilliant, even after 40 minutes plating time.
In addition to the examples detailed above, satisfactory deposits were obtained from baths containing the following alternative ingredients.
A. Conducting salts: potassium sulfate, potassium nitrate,
sodium glycolate B. Chelating agents: pyridine diethylethanol amine, 2,4-
lutidine, triethylene tetramine, and
C. Silver salts: silver fluoride, silver acetate.
In all cases, the silver ion was responsible for the bright deposits obtained, and the best deposits and most stable bath resulted when a compound capable of chelating silver was present in the bath.
The above baths were normally operated at room temperature, but they can be operated up to a temperature of 45 C. Above this temperature hazy deposits are apt to be obtained. The baths can be operated at temperatures down to about 15 C.
The normal current density range is 1 to 5 a.s.f. (0.1O.5 amp/43m?) depending upon the gold content, the temperature, and the rate of agitation. At higher temperatures, high gold content and very vigorous agitation, considerably higher current densities can be employed, but the control of commercial baths becomes somewhat more critical.
In general, agitation, either solution volume or mechanical agitation is useful and, actually air agitation is etleetive for this bath in contrast to high free cyanide gold baths where the ethciency drops rapidly when air agitation is used.
Obviously, current knowledge will suggest adaptation of the method of this invention and such adaptations should be comprehended within the meaning of this invention.
We claim:
1. An aqueous electrolyte for the production of bright gold deposits consisting essentially of the following ingredients:
KAu(CN) (calculated as Au) 4 to 20 g./l. KAg(CN) (calculated as Ag) 25 to 500 mg./l. Alkali metal conducting salt (other than cyanide) 5 to g./l. Alkali hydroxide to pH 6.513. Triglycollamic acid 5 to 10 g./l.
the proportion of triglycollamic acid within said limits increasing as the amount of silver is increased within said limits.
2. An aqueous electrolyte for the production of bright gold deposits consisting essentially of the following ingredients:
the proportion of disodium EDTA within said limits increasing as the amount of silver is increased within said limits.
References Cited in the file of this patent UNITED STATES PATENTS Ostrow Nov. 24, 1953 Ostrow et al Jan. 3, 1961

Claims (2)

1. AN AQUEOUS ELECTROLYTE FOR THE PRODUCTION OF BRIGHT GOLD DEPOSITS CONSISTING ESSENTIALLY OF THE FOLLOWING INGREDIENTS:
2. AN AQUEOUS ELECTROLYTE FOR THE PRODUCTION OF BRIGHT GOLD DEPOSITS CONSISTING ESSENTIALLY OF THE FOLLOWING INGREDIENTS:
US84517A 1961-01-24 1961-01-24 Bright gold electroplating Expired - Lifetime US3174918A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
NL273924D NL273924A (en) 1961-01-24
CH51162A CH399865A (en) 1961-01-24 1957-10-02 Electrolytic gold deposition process making it possible to obtain deposits of brilliant gold, and electrolyte for the implementation of this process
US84517A US3174918A (en) 1961-01-24 1961-01-24 Bright gold electroplating
GB45060/61A GB939007A (en) 1961-01-24 1961-12-15 Bright gold electroplating
FR885252A FR1311023A (en) 1961-01-24 1962-01-18 Electrolytic gold deposition process making it possible to obtain deposits of brilliant gold, and electrolyte for the implementation of this process

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US84517A US3174918A (en) 1961-01-24 1961-01-24 Bright gold electroplating

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FR (1) FR1311023A (en)
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NL (1) NL273924A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3362895A (en) * 1964-11-23 1968-01-09 Sel Rex Corp Electrodeposition of silver
US3902977A (en) * 1973-12-13 1975-09-02 Engelhard Min & Chem Gold plating solutions and method
US4024031A (en) * 1975-10-28 1977-05-17 Amp Incorporated Silver plating
US4168214A (en) * 1978-06-14 1979-09-18 American Chemical And Refining Company, Inc. Gold electroplating bath and method of making the same
EP0241582A2 (en) * 1982-10-29 1987-10-21 WAHLBECK, Hans G.E. Method for the manufacture of non-allergy creating precious metal objects.
JP2008133533A (en) * 2006-11-01 2008-06-12 Ne Chemcat Corp Gold-silver alloy plating liquid
ITFI20120103A1 (en) * 2012-06-01 2013-12-02 Bluclad Srl GALVANIC BATHROOMS FOR THE ACHIEVEMENT OF A LEAGUE OF LOW-CARATHED GOLD AND GALVANIC PROCESS THAT USES THESE BATHROOMS.

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3406107A (en) * 1964-12-07 1968-10-15 Ibm Non-cyanide silver plating bath
GB1294309A (en) 1969-01-15 1972-10-25 Pmd Chemicals Ltd Electrodeposition of gold
DE2355581C3 (en) * 1973-11-07 1979-07-12 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt Galvanic bright gold bath with high deposition rate

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2660554A (en) * 1950-11-10 1953-11-24 Barnet D Ostrow Bright gold and gold alloy plating baths
US2967135A (en) * 1960-06-08 1961-01-03 Barnet D Ostrow Electroplating baths for hard bright gold deposits

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2660554A (en) * 1950-11-10 1953-11-24 Barnet D Ostrow Bright gold and gold alloy plating baths
US2967135A (en) * 1960-06-08 1961-01-03 Barnet D Ostrow Electroplating baths for hard bright gold deposits

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3362895A (en) * 1964-11-23 1968-01-09 Sel Rex Corp Electrodeposition of silver
US3902977A (en) * 1973-12-13 1975-09-02 Engelhard Min & Chem Gold plating solutions and method
US4024031A (en) * 1975-10-28 1977-05-17 Amp Incorporated Silver plating
US4168214A (en) * 1978-06-14 1979-09-18 American Chemical And Refining Company, Inc. Gold electroplating bath and method of making the same
EP0241582A2 (en) * 1982-10-29 1987-10-21 WAHLBECK, Hans G.E. Method for the manufacture of non-allergy creating precious metal objects.
EP0241582A3 (en) * 1982-10-29 1990-01-31 Hans G.E. Wahlbeck Method and apparatus for the manufacture of non-allergy creating precious metal objects
JP2008133533A (en) * 2006-11-01 2008-06-12 Ne Chemcat Corp Gold-silver alloy plating liquid
ITFI20120103A1 (en) * 2012-06-01 2013-12-02 Bluclad Srl GALVANIC BATHROOMS FOR THE ACHIEVEMENT OF A LEAGUE OF LOW-CARATHED GOLD AND GALVANIC PROCESS THAT USES THESE BATHROOMS.
EP2669407A1 (en) * 2012-06-01 2013-12-04 Bluclad S.R.L. Galvanic baths for obtaining a low-carat gold alloy, and galvanic process that uses said baths

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Publication number Publication date
FR1311023A (en) 1962-11-30
NL273924A (en)
GB939007A (en) 1963-10-09
CH399865A (en) 1965-09-30

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