US20160145745A1 - Formaldehyde-free electroless metal plating compositions and methods - Google Patents

Formaldehyde-free electroless metal plating compositions and methods Download PDF

Info

Publication number
US20160145745A1
US20160145745A1 US14/552,478 US201414552478A US2016145745A1 US 20160145745 A1 US20160145745 A1 US 20160145745A1 US 201414552478 A US201414552478 A US 201414552478A US 2016145745 A1 US2016145745 A1 US 2016145745A1
Authority
US
United States
Prior art keywords
acid
salts
alkyl
substituted
unsubstituted
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.)
Abandoned
Application number
US14/552,478
Other languages
English (en)
Inventor
Weigang Wu
Crystal P. L. LI
Zhixiong LIANG
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.)
Rohm and Haas Electronic Materials LLC
Original Assignee
Rohm and Haas Electronic Materials LLC
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 Rohm and Haas Electronic Materials LLC filed Critical Rohm and Haas Electronic Materials LLC
Priority to US14/552,478 priority Critical patent/US20160145745A1/en
Assigned to ROHM AND HAAS ELECRONIC MATERIALS LLC reassignment ROHM AND HAAS ELECRONIC MATERIALS LLC ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: Li, Crystal P.L., LIANG, Zhixiong, WU, WEIGANG
Priority to EP15193850.3A priority patent/EP3023515A3/en
Priority to TW104137388A priority patent/TWI655319B/zh
Priority to JP2015224151A priority patent/JP6138892B2/ja
Priority to KR1020150163009A priority patent/KR101739421B1/ko
Priority to CN201510809868.0A priority patent/CN105624653B/zh
Publication of US20160145745A1 publication Critical patent/US20160145745A1/en
Abandoned legal-status Critical Current

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31—Coating with metals
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/18—Pretreatment of the material to be coated
    • C23C18/1851—Pretreatment of the material to be coated of surfaces of non-metallic or semiconducting in organic material
    • C23C18/1872—Pretreatment of the material to be coated of surfaces of non-metallic or semiconducting in organic material by chemical pretreatment
    • C23C18/1886—Multistep pretreatment
    • C23C18/1893—Multistep pretreatment with use of organic or inorganic compounds other than metals, first
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31—Coating with metals
    • C23C18/32—Coating with nickel, cobalt or mixtures thereof with phosphorus or boron
    • C23C18/34—Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31—Coating with metals
    • C23C18/38—Coating with copper
    • C23C18/40—Coating with copper using reducing agents
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31—Coating with metals
    • C23C18/42—Coating with noble metals
    • C23C18/44—Coating with noble metals using reducing agents
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/48—Coating with alloys
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/48—Coating with alloys
    • C23C18/50—Coating with alloys with alloys based on iron, cobalt or nickel
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/52—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating using reducing agents for coating with metallic material not provided for in a single one of groups C23C18/32 - C23C18/50
    • C—CHEMISTRY; METALLURGY
    • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C30/00—Coating with metallic material characterised only by the composition of the metallic material, i.e. not characterised by the coating process
    • H—ELECTRICITY
    • H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
    • H05K3/00—Apparatus or processes for manufacturing printed circuits
    • H05K3/10—Apparatus or processes for manufacturing printed circuits in which conductive material is applied to the insulating support in such a manner as to form the desired conductive pattern
    • H05K3/18—Apparatus or processes for manufacturing printed circuits in which conductive material is applied to the insulating support in such a manner as to form the desired conductive pattern using precipitation techniques to apply the conductive material
    • H05K3/181—Apparatus or processes for manufacturing printed circuits in which conductive material is applied to the insulating support in such a manner as to form the desired conductive pattern using precipitation techniques to apply the conductive material by electroless plating
    • H05K3/187—Apparatus or processes for manufacturing printed circuits in which conductive material is applied to the insulating support in such a manner as to form the desired conductive pattern using precipitation techniques to apply the conductive material by electroless plating means therefor, e.g. baths, apparatus

Definitions

  • the present invention is directed to environmentally friendly, formaldehyde-free electroless metal plating compositions and methods containing glyoxylic acid and salts thereof and tertiary amines. More specifically, the present invention is directed to environmentally friendly, formaldehyde-free electroless metal plating compositions and methods containing glyoxylic acid and salts thereof and tertiary amines to inhibit decomposition of the glyoxylic acid and salts thereof.
  • Electroless metal plating compositions such as electroless copper plating compositions are in widespread use in metallization industries for depositing copper and other metals on various types of substrates.
  • the electroless copper baths are used to deposit copper into through-holes and circuit paths as a base for subsequent electrolytic copper plating.
  • Electroless copper and other electroless metal plating compositions also are used in the decorative plastics industry for deposition of metals onto non-conductive surfaces as a base for further plating of copper, nickel, gold, silver and other metals as required.
  • Typical electroless copper plating baths which are in commercial use today contain divalent copper compounds, chelating agents or complexing agents for the divalent copper ions, formaldehyde reducing agents and various addition agents to make the bath more stable, adjust the plating rate and brighten the copper deposit. Although many of such baths are successful and are widely used, the metallization industry has been searching for alternative electroless copper plating baths that do not contain formaldehyde due to its toxic nature.
  • Formaldehyde is known as an eye, nose and upper respiratory tract irritant. Animal studies have shown that formaldehyde is an in vitro mutagen. According to a WATCH committee report (WATCH/2005/06—Working group on Action to Control Chemicals—sub committee with UK Health and Safety Commission) over fifty epidemiological studies have been conducted prior to 2000 suggested a link between formaldehyde and nasopharyngeal/nasal cancer but were not conclusive. However, more recent studies conducted by IARC (International Agency for Research on Cancer) in the U.S.A. showed that there was sufficient epidemiological evidence that formaldehyde causes nasopharyngeal cancer in humans.
  • IARC International Agency for Research on Cancer
  • glyoxylic acid or its salts have a high decomposition rate which compromises its performance as an acceptable substitute for formaldehyde.
  • One of the most likely decomposition pathways is the Cannizzaro reaction:
  • Cannizzaro reaction may be inhibited by including certain molar amounts of methanol, primary amines, secondary amines, metasilicic acid and its salts, phosphoric acid and its salts, germanium dioxide, vanadic acid and its salts in the electroless copper plating solution.
  • U.S. 2003/0183120 alleges that including succinic acid in the electroless copper plating solution may inhibit the Cannizzaro reaction.
  • Compositions include one or more sources of metal ions, one or more sources of glyoxylic acid, salts or mixtures thereof and one or more tertiary amine compounds, salts or halides thereof having a formula:
  • R 1 , R 2 and R 3 may be the same or different and are linear or branched, substituted or unsubstituted hydroxy(C 1 -C 10 )alkyl, linear or branched, substituted or unsubstituted carboxy(C 1 -C 10 )alkyl, linear or branched, substituted or unsubstituted (C 1 -C 10 )alkylamine, linear or branched, substituted or unsubstituted (C 1 -C 10 )alkyl phosphonic acid or a moiety having a formula:
  • R 4 and R 5 may be the same or different and are linear or branched, substituted or unsubstituted hydroxy(C 1 -C 10 )alkyl, linear or branched, substituted or unsubstituted carboxy(C 1 -C 10 )alkyl, linear or branched, substituted or unsubstituted (C 1 -C 10 )alkylamine, linear or branched, substituted or unsubstituted (C 1 -C 10 )alkyl phosphonic acid, or moiety —(CH 2 ) a —N—((CH 2 ) b ) 2 —(P(O)(OH) 2 ) (IIa) where a and b may be the same or different and are integers of 1 to 6, m is an integer from 1 to 6, B is a moiety having a formula:
  • A is a chemical bond with the nitrogen of formula (I) or a moiety having a formula:
  • R 8 , R 9 , R 10 and R 11 are the same or different and are hydrogen, hydroxyl or (C 1 -C 3 )alkyl, n, p, q may be the same or different and are integers of 1 to 6, with the proviso that when any two of R 1 , R 2 and R 3 are carboxymethyl moieties or salts thereof the third cannot be formula (II) where A is a chemical bond, B is formula (IIb), m is 2, R 6 and R 7 are hydrogen and R 4 and R 5 are carboxymethyl moieties or salts thereof; and a molar ratio of the one or more tertiary amine compounds to the glyoxylic acid or salts thereof is 0.05:1 to 15:1, the compositions are formaldehyde-free.
  • Methods include providing a substrate and applying the composition including the one or more sources of metal ions, glyoxylic acid, salts or mixtures thereof and one or more of the tertiary amines, salts, halides or mixtures thereof to the substrate; and electroless plating copper on the substrate.
  • the combination of the one or more tertiary amines and glyoxylic acid, salts or mixtures thereof provide a stable electroless metal plating composition which is formaldehyde-free and environmentally friendly.
  • the tertiary amines inhibit the decomposition of glyoxylic acids and its salts, thus prolonging the life of the plating composition and reducing the cost of the operation of the plating composition as replacement with glyoxylic acid or its salts is reduced or eliminated.
  • the combination of the one or more tertiary amines, salts, halides or mixtures thereof and the glyoxylic acid, salts or mixtures thereof at the molar ratios provides for a more efficient electroless metal plating process than many conventional electroless metal compositions and plating processes.
  • the plating compositions may provide for substantially uniform, bright metal deposits on substrates and reduced skip plating.
  • FIGURE illustrates the European Backlight Reference Plates for determining metal plating coverage performance of through-holes of printed circuit boards for electroless copper plating.
  • printed circuit board and “printed wiring board” are synonymous.
  • plating and “deposition” are used interchangeably throughout this specification.
  • moiety means a part of a molecule or polymer that may include either whole functional groups or parts of functional groups as substructures.
  • halide means chloride, bromide, fluoride or iodide. All amounts are percent by weight, unless otherwise noted. All numerical ranges are inclusive and combinable in any order except where it is logical that such numerical ranges are constrained to add up to 100%.
  • Aqueous based electroless metal plating compositions include one or more sources of metal ions, glyoxylic acid, salts of glyoxylic acid or mixtures thereof as reducing agents for the metal ions and one or more tertiary amine compounds, salts and halides thereof having a formula:
  • R 1 , R 2 and R 3 may be the same or different and are linear or branched, substituted or unsubstituted hydroxy(C 1 -C 10 )alkyl, linear or branched, substituted or unsubstituted carboxy(C 1 -C 10 )alkyl, linear or branched, substituted or unsubstituted (C 1 -C 10 )alkylamine, linear or branched, substituted or unsubstituted (C 1 -C 10 )alkyl phosphonic acid or a moiety having a formula:
  • R 4 and R 5 may be the same or different and are linear or branched, substituted or unsubstituted hydroxy(C 1 -C 10 )alkyl, linear or branched, substituted or unsubstituted carboxy(C 1 -C 10 )alkyl, linear or branched, substituted or unsubstituted (C 1 -C 10 )alkylamine, linear or branched, substituted or unsubstituted (C 1 -C 10 )alkyl phosphonic acid, or moiety —(CH 2 ) a —N—((CH 2 ) b ) 2 —(P(O)(OH) 2 ) (IIa) where a and b may be the same or different and are integers of 1 to 6, m is an integer from 1 to 6, B is a moiety having formula:
  • A is a chemical bond with the nitrogen of formula (I) or a moiety having a formula:
  • R 8 , R 9 , R 10 and R 11 are the same or different and are hydrogen, hydroxyl or (C 1 -C 3 )alkyl, n, p and q may be the same or different and are integers of 1 to 6, with the proviso that when any two of R 1 , R 2 and R 3 are carboxymethyl moieties or salts thereof the third cannot be formula (II) where A is a chemical bond, B is formula (IIb), m is 2, R 6 and R 7 are hydrogen and R 4 and R 5 are carboxymethyl moieties or salts thereof; and a molar ratio of the one or more tertiary amine compounds to the glyoxylic acid or salts thereof is 0.05:1 to 15:1.
  • R 1 , R 2 and R 3 may be the same or different and are linear or branched, substituted or unsubstituted hydroxy(C 1 -C 6 )alkyl, linear or branched, substituted or unsubstituted carboxy(C 1 -C 6 )alkyl, linear or branched, substituted or unsubstituted (C 1 -C 6 )alkylamine, linear or branched, substituted or unsubstituted (C 1 -C 6 )alkyl phosphonic acid or a moiety having a formula:
  • R 4 and R 5 may be the same or different and are linear or branched, substituted or unsubstituted hydroxy(C 1 -C 6 )alkyl, linear or branched, substituted or unsubstituted carboxy(C 1 -C 6 )alkyl, linear or branched, substituted or unsubstituted (C 1 -C 6 )alkylamine, linear or branched, substituted or unsubstituted (C 1 -C 6 )alkyl phosphonic acid, or moiety —(CH 2 ) a —N—((CH 2 ) b ) 2 —P(O)(OH) 2 ) (IIa) where a and b may be the same or different and are integers of 1 to 3, m is an integer from 1 to 3, R 6 and R 7 may be the same or different and are hydrogen, hydroxyl, carboxyl, hydroxy(C 1 -C 2 )alkyl, carboxy(C 1 -C 2
  • R 8 , R 9 , R 10 and R 11 are the same or different and are hydrogen, hydroxyl or (C 1 -C 2 )alkyl, n, p, q may be the same or different and are integers of 1 to 3.
  • R 1 , R 2 and R 3 may be the same or different and are linear or branched, substituted or unsubstituted hydroxy(C 1 -C 4 )alkyl, linear or branched, substituted or unsubstituted carboxy(C 1 -C 4 )alkyl, linear or branched, substituted or unsubstituted (C 1 -C 4 )alkylamine, linear or branched, substituted or unsubstituted (C 1 -C 4 )alkyl phosphonic acid or a moiety having a formula:
  • R 4 and R 5 may be the same or different and are hydroxy(C 1 -C 3 )alkyl, carboxy(C 1 -C 3 )alkyl, m is an integer from 2 to 3, R 6 and R 7 may be the same or different and are hydrogen, hydroxyl, carboxyl, (C 1 -C 2 )alkyl, and A is a chemical bond with the nitrogen of formula (I).
  • Salts of the foregoing tertiary amine compounds include, but are not limited to alkali metal salts, such as potassium, sodium and lithium salts and ammonium salts.
  • the salts are alkali metal salts such as potassium and sodium, more preferably the salt is sodium.
  • Halides are Cl ⁇ , F ⁇ , Br ⁇ and I ⁇ .
  • Sources of halides include, but are not limited to hydrogen chloride, hydrogen bromide, hydrogen fluoride and hydrogen iodide.
  • the source of halides is hydrogen chloride.
  • Substituent groups include, but are not limited to hydroxyl, linear or branched hydroxy(C 1 -C 4 )alkyl, carboxyl, linear or branched carboxy(C 1 -C 4 )alkyl, linear or branched (C 1 -C 4 )alkyl or an amine moiety having formula:
  • R 12 and R 13 may be the same or different and are hydrogen or linear or branched (C 1 -C 4 )alkyl, hydroxy(C 1 -C 3 )alkyl, carboxy(C 1 -C 3 )alkyl and d is an integer of 1 to 3.
  • substituent groups are hydroxyl, carboxyl or (C 1 -C 3 )alkyl.
  • tertiary amines are triethanolamine, 2-[bis(2-hydroxyethyl)amino]acetic acid and its salts, N-(2-hydroxyethyl)iminodiacetic acid and its salts, nitrilotriacetic acid, nitrile(3-propionic)diacetic acid and its salts, nitriltripropionic acid and its salts, N,N-bis(2-hydroxypropyl)ethanolamine, 1-[bis(2-hydroxyethyl)amino]-2-propanol, 2-[bis(2-hydroxyethyl)amino]-2-(hydroxymethyl)-1,3-propanediol, N,N-Bis(carboxymethyl)-DL-alanine and its salts, triisopropanolamine, L-glutamic acid N,N′-diacetic acid and its salts, N,N,N′,N′-tetrakis(2-hydroxypropyl)
  • the electroless plating compositions are formaldehyde-free, thus enabling environmentally friendly electroless metal plating compositions.
  • the tertiary amines suppress unwanted decomposition of glyoxylic acid and its salts to provide a more efficient and reliable electroless plating composition.
  • the compositions are also free of ethylenediamine tetraacetic acid and its salts.
  • Sources of glyoxylic acid include non-dissociated glyoxylic acid, salts of glyoxylic acid such as alkali metal salts of glyoxylic acid, such as sodium and potassium salts, and those reducing agents that can provide glyoxylate ions in an alkaline solution such as dihydroxy acetic acid, a dihaloacetic acid and the bisulphite adduct of glyoxylic acid.
  • the source of the reducing agent is glyoxylic acid.
  • the concentration range may be from 0.1 g/L to 100 g/L, preferably from 1 g/L to 50 g/L.
  • the amount of the tertiary amine included in the electroless compositions is based on a molar ratio of tertiary amine to glyoxylic acid.
  • the molar ratio of the tertiary amine suppressor to glyoxylic acid in the electroless composition is in a range of 0.05:1 to 15:1. When the molar ratio is lower than 0.05:1, the suppressor does not effectively suppress glyoxylic acid decomposition. When the molar ratio is greater than 15:1, the suppressor substantially hinders plating performance.
  • the molar ratio of tertiary amine to glyoxylic acid is 0.2:1 to 10:1, more preferably 0.4:1 to 10:1.
  • Metals which may be plated include, but are not limited to copper, gold, silver, nickel and tin.
  • the metals are copper, tin and nickel, more preferably the metals are copper and nickel. Most preferably the metal is copper.
  • Alloys which may be plated include but are not limited to binary alloys such as copper/tin and copper nickel alloys and ternary alloys such as copper/tin/silver.
  • Conventional sources of metal ions which are soluble in an aqueous medium may be used.
  • Conventional amounts of metal ions for electroless plating may be used.
  • Sources of copper ions include, but are not limited to water soluble halides, nitrates, acetates, sulfates and other organic and inorganic salts of copper. Mixtures of one or more of such copper salts may be used to provide copper ions. Examples include copper sulfate, such as copper sulfate pentahydrate, copper chloride, copper nitrate, copper sulfamate, copper hydroxide, and copper methane sulfonate ((CH 3 O 3 S) 2 Cu). Copper ion concentrations in the composition may range from 0.25 g/L to 30 g/L or such as from 0.5 g/L to 20 g/L or such as from 1 g/L to 10 g/L.
  • Sources of nickel ions include, but are not limited to nickel sulfate, nickel chloride, nickel sulfamate, and nickel phosphate. Mixtures of nickel compounds may be used in the plating compositions. The nickel compounds may be added to the plating compositions in amounts sufficient to provide a nickel ion concentration in the plating composition of 0.1 g/L to 50 g/L, or such as 0.5 g/L to 30 g/L, or such as 1 g/L to 20 g/L.
  • Sources of tin ions include, but are not limited to salts, such as tin halides, tin sulfates, tin alkane sulfonates, tin alkanol sulfonates, and acids.
  • tin halide it is typical that the halide is chloride.
  • the tin compound is typically tin sulfate, tin chloride or a tin alkane sulfonate, and more typically tin sulfate or tin methane sulfonate.
  • Sufficient amounts of tin salts are added to the electroless composition to provide tin (II) ions in amounts of 0.5 g/L to 80 g/L, typically from 5 g/L to 50 g/L.
  • Sources of silver ions may be provided by silver salts such as, but are not limited to silver halides, silver gluconate, silver citrate, silver lactate, silver nitrate, silver sulfates, silver alkane sulfonates and silver alkanol sulfonates. When a silver halide is used, it is typical that the halide is chloride.
  • the silver salts are silver sulfate, a silver alkane sulfonate or mixtures thereof, and more typically silver sulfate, silver methane sulfonate or mixtures thereof.
  • Sufficient amounts of silver salts are added to the electroless plating composition to provide silver ions in amounts of 0.01 g/L to 60 g/L, typically from 0.02 g/L to 30 g/L.
  • Sources of gold ions include, but are not limited to one or more gold salts which provide gold (I) ions.
  • Such sources of gold (I) ions include, but are not limited to alkali gold cyanide compounds such as potassium gold cyanide, sodium gold cyanide, and ammonium gold cyanide, alkali gold thiosulfate compounds such as trisodium gold thiosulfate and tripotassium gold thiosulfate, alkali gold sulfite compounds such as sodium gold sulfite and potassium gold sulfite, ammonium gold sulfite, and gold (I) and gold (III) halides such as gold (I) chloride and gold (III) trichloride.
  • gold sources are added to the electroless plating compositions to provide gold ion concentrations of 0.5 g/L to 50 g/L, or such as from 5 g/L to 30 g/L, or such as from 10 g/L to 20 g/L.
  • the electroless metal plating composition may include one or more optional additives to tailor the compositions to a desired plating performance for a given application.
  • optional additives include, but are not limited to accelerators, uniformity enhancers, stabilizers, grain-refiners, complexing agents, chelating agents, additional reducing agents, pH adjusting agents, antioxidants and surfactants.
  • Uniformity enhancers with an ability to enhance the initiation of electroless plating include but are not limited to aldehydes such as glyoxal, succindialdehyde, glucose and acetaldehyde. Such aldehydes may be included in the electroless metal plating compositions in amounts of 0.01 g/L to 10 g/L, preferably from 0.5 g/l to 5 g/L.
  • one or more additional reducing agents may include, but are not limited to hypophosphite, glycolic acid, glyoxal, ascorbic acid, formic acid and glycine.
  • the additional reducing agents may be used in their conventional amounts.
  • Complexing agents include, but are not limited to ethylenediamine-N,N′-disuccinic acid (EDDS) and its salts, Rochelle salts, potassium tartrate, citric acid and its salts, ethanoldiamine, Iminodiacetic acid and its salts, pyrophosphoric acid and its salts, salicylic acid and its salts, hydroxyethylidene diphosphonic acid and its salts, xylitol and D-sorbitol.
  • the molar ratio of complexing agents to metal ions may range from 0.5:1 to 50:1 or such as from 1:1 to 15:1 or such as from 1.2:1 to 8:1.
  • Stabilizers include, but are not limited to sulfur containing compounds such as 2-mercaptopyridine, 2-mercaptobenzothiazole, 2-mercaptothiazoline, mercaptobenzothiazole, thiourea and its derivatives; cyanides such as KCN, NaCN, K 4 [Fe(CN) 6 ], thiocyanates; dipyridyls and its derivatives such as 2,2′-dipyridyl, methylpiperidine, 1,2-di-(2-pyridyl)ethylene, 2,2′-dipyridylamine, pyridazine, 6,6′-dimethyl-2,2′dipyridyl, di-2-pyrylketone and 2,2′-bipyrimidine. Such stabilizers may be included in amounts of 1 ppm to 10 g/L.
  • Optional grain-refining additives include, but are not limited to high molecular weight polymer compounds such as polyalkylene glycols, polyacrylamides, poly acrylates, polypropylene glycols, polyethylene glycols (PEG). Some are available in various molecular weights such as PEG which may be available as PEG 600, PEG 2000, PEG 4000, PEG 6000 and PEG 10000.
  • the grain-refining additives are included in amounts of 0.1 ppm to 300 ppm, preferably 1 ppm to 100 ppm.
  • Rate-accelerating additives include, but are not limited to sulfur-based organic molecules such as bis(sodium sulfopropyl)disulfide, sodium 3-(benzothiazol-2-ylthio)-1-propanesulfonate and other disulfides. Such compounds are included in amounts of 0.1 ppm to 30 ppm, preferably from 0.5 ppm to 10 ppm.
  • Other rate accelerating additives include, but are not limited to ammonia, ethylenediamine and mannitol. Such rate-accelerating compounds may be included in amounts of 0.01 g/L to 5 g/L.
  • the pH of the composition is adjusted by one or more alkaline compounds chosen from lithium hydroxide, sodium hydroxide, potassium hydroxide and ammonium hydroxide to provide a pH greater than 7, typically 8 and greater.
  • alkaline compounds chosen from lithium hydroxide, sodium hydroxide, potassium hydroxide and ammonium hydroxide to provide a pH greater than 7, typically 8 and greater.
  • organic alkalis such as tetramethyl ammonium hydroxide (TMAH) are used for pH adjustment to avoid the introduction of alkaline metal ions onto the surface or into the plated copper coating.
  • TMAH tetramethyl ammonium hydroxide
  • sodium hydroxide, potassium hydroxide and TMAH or mixtures thereof are used.
  • potassium hydroxide is used because potassium oxalate has a higher solubility than that of sodium oxalate.
  • the potassium hydroxide concentration is from 3 g/L to 100 g/L, more preferably from 10 g/L to 80 g/L.
  • a preferred pH range of the electroless metal compositions is from 10 to 14, more preferably from 11.5 to 13.5, most preferably from 12.5 to 13.5.
  • surfactants may be included in the compositions.
  • Such surfactants include ionic, such as cationic and anionic surfactants, non-ionic and amphoteric surfactants. Mixtures of the surfactants may be used.
  • surfactants may be included in conventional amounts for electroless copper plating compositions.
  • Surfactants may be included in the compositions in amounts of 0.001 g/L to 50 g/L.
  • Cationic surfactants include, but are not limited to tetra-alkylammonium halides, alkyltrimethylammonium halides, hydroxyethyl alkyl imidazoline, alkylbenzalkonium halides, alkylamine acetates, alkylamine oleates and alkylaminoethyl glycine.
  • Anionic surfactants include, but are not limited to alkylbenzenesulfonates, alkyl or alkoxy naphthalene sulfonates, alkyldiphenyl ether sulfonates, alkyl ether sulfonates, alkylsulfuric esters, polyoxyethylene alkyl ether sulfuric esters, polyoxyethylene alkyl phenol ether sulfuric esters, higher alcohol phosphoric monoesters, polyoxyalkylene alkyl ether phosphoric acids (phosphates) and alkyl sulfosuccinates.
  • Amphoteric surfactants include, but are not limited to 2-alkyl-N-carboxymethyl or ethyl-N-hydroxyethyl or methyl imidazolium betaines, 2-alkyl-N-carboxymethyl or ethyl-N-carboxymethyloxyethyl imidazolium betaines, dimethylalkyl betains, N-alkyl- ⁇ -aminopropionic acids or salts thereof and fatty acid amidopropyl dimethylaminoacetic acid betaines.
  • Non-ionic surfactants include, but are not limitted to are alkyl phenoxy polyethoxyethanols, polyoxyethylene polymers having from 20 to 150 repeating units and block and random copolymers of polyoxyethylene and polyoxypropylene.
  • Antioxidants include, but are not limited to monohydric, dihydric and trihydric phenols in which a hydrogen atom or atoms may be unsubstituted or substituted by —COOH, —SO 3 H, lower alkyl or lower alkoxy groups, hydroquinone, catechol, resorcinol, quinol, pyrogallol, hydroxyquinol, phloroglucinol, guaiacol, gallic acid, 3,4-dihydroxybenzoic acid, phenolsulfonic acid, cresolsulfonic acid, hydroquinonsulfonic acid, catecholsulfonic acid and salts thereof.
  • Antioxidants may be included in the compositions in conventional amounts typically used for electroless copper compositions such as from 1 ppm to 1000 ppm.
  • the electroless metal compositions may be used to deposit a metal on both conductive and non-conductive substrates.
  • the electroless compositions may be used in many conventional methods known in the art. Typically copper deposition is done at temperatures of 20° C. to 80° C. Preferably the electroless compositions deposit copper at temperatures of 20° C. to 60° C.
  • the substrate to be plated with copper is immersed in the electroless composition or the electroless composition is sprayed onto the substrate. Conventional plating times may be used to deposit the copper onto the substrate. Deposition may be done for 5 seconds to 30 minutes; however, plating times may vary depending on the thickness of the metal desired on the substrate and the plating bath temperature. Metal plating rates may range from 0.15 ⁇ m/5 minutes to 0.5 ⁇ m/5 minutes, preferably from 0.25 ⁇ m/5 minutes to 0.45 ⁇ m/5 minutes.
  • Substrates include, but are not limited to materials including inorganic and organic substances such as glass, ceramics, porcelain, resins, paper, cloth and combinations thereof.
  • Metal-clad and unclad materials also are substrates which may be plated with the electroless copper compositions.
  • Substrates also include printed circuit boards.
  • Such printed circuit boards include metal-clad and unclad with thermosetting resins, thermoplastic resins and combinations thereof, including fiber, such as fiberglass, and impregnated embodiments of the foregoing.
  • Thermoplastic resins include, but are not limited to acetal resins, acrylics, such as methyl acrylate, cellulosic resins, such as ethyl acetate, cellulose propionate, cellulose acetate butyrate and cellulose nitrate, polyethers, nylon, polyethylene, polystyrene, styrene blends, such as acrylonitrile styrene and copolymers and acrylonitrile-butadiene styrene copolymers, polycarbonates, polychlorotrifluoroethylene, and vinylpolymers and copolymers, such as vinyl acetate, vinyl alcohol, vinyl butyral, vinyl chloride, vinyl chloride-acetate copolymer, vinylidene chloride and vinyl formal.
  • acetal resins acrylics, such as methyl acrylate
  • cellulosic resins such as ethyl acetate, cellulose propionate, cellulose acetate butyrate and
  • Thermosetting resins include, but are not limited to allyl phthalate, furane, melamine-formaldehyde, phenol-formaldehyde and phenol-furfural copolymers, alone or compounded with butadiene acrylonitrile copolymers or acrylonitrile-butadiene-styrene copolymers, polyacrylic esters, silicones, urea formaldehydes, epoxy resins, allyl resins, glyceryl phthalates and polyesters.
  • Porous materials include, but are not limited to paper, wood, fiberglass, cloth and fibers, such as natural and synthetic fibers, such as cotton fibers and polyester fibers.
  • the electroless copper compositions may be used to plate both low and high T g resins.
  • Low T g resins have a T g below 160° C. and high T g resins have a T g of 160° C. and above.
  • high T g resins have a T g of 160° C. to 280° C. or such as from 170° C. to 240° C.
  • High T g polymer resins include, but are not limited to polytetrafluoroethylene (PTFE) and polytetrafluoroethylene blends. Such blends include, for example, PTFE with polypheneylene oxides and cyanate esters.
  • polymer resins which include resins with a high T g include, but are not limited to: epoxy resins, such as difunctional and multifunctional epoxy resins, bimaleimide/triazine and epoxy resins (BT epoxy), epoxy/polyphenylene oxide resins, acrylonitrile butadienestyrene, polycarbonates (PC), polyphenylene oxides (PPO), polypheneylene ethers (PPE), polyphenylene sulfides (PPS), polysulfones (PS), polyamides, polyesters such as polyethyleneterephthalate (PET) and polybutyleneterephthalate (PBT), polyetherketones (PEEK), liquid crystal polymers, polyurethanes, polyetherimides, epoxies and composites thereof.
  • epoxy resins such as difunctional and multifunctional epoxy resins, bimaleimide/triazine and epoxy resins (BT epoxy), epoxy/polyphenylene oxide resins, acrylonitrile butadienestyren
  • the electroless compositions may be used to deposit copper on walls of through-holes or vias of printed circuit board substrates as well as other parts of the boards.
  • the electroless compositions may be used in both horizontal and vertical processes of manufacturing printed circuit boards.
  • the boards may be rinsed with water and cleaned and degreased followed by desmearing the through-hole walls.
  • prepping or softening the dielectric or desmearing of the through-holes begins with application of a solvent swell.
  • Any conventional solvent swell may be used. The specific type may vary depending on the type of dielectric material. Minor experimentation may be done to determine which solvent swell is suitable for a particular dielectric material.
  • Solvent swells include, but are not limited to glycol ethers and their associated ether acetates.
  • CIRCUPOSITTM Conditioner 3302A examples of commercially available solvent swells are CIRCUPOSITTM Conditioner 3302A, CIRCUPOSITTM MLB Conditioner 211, CIRCUPOSITTM Hole Prep 3303 and CIRCUPOSITTM Hole Prep 4120 solutions (available from Dow Electronic Materials).
  • a promoter may be applied.
  • Conventional promoters may be used.
  • Such promoters include sulfuric acid, chromic acid, alkaline permanganate or plasma etching. Typically alkaline permanganate is used as the promoter.
  • Examples of commercially available promoters are CIRCUPOSITTM Promoter 4130, CIRCUPOSITTM MLB Promoter 213-A and CIRCUPOSITTM MLB Promoter 3308 solutions (available from Dow Electronic Materials).
  • the substrate and through-holes are rinsed with water.
  • a neutralizer may then be applied to neutralize any residues left by the promoter.
  • Conventional neutralizers may be used.
  • the neutralizer is an aqueous acidic solution containing one or more amines or a solution of 3 wt % hydrogen peroxide and 3 wt % sulfuric acid.
  • An example of a commercially available neutralizer is CIRCUPOSITTM MLB Neutralizer 216-5.
  • the substrate and through-holes are rinsed with water and then dried.
  • conditioners may be used. Such conditioners may include one or more cationic surfactants, non-ionic surfactants, complexing agents and pH adjusters or buffers. Examples of commercially available acid conditioners are CIRCUPOSITTM Conditioners 3320A and 3327 solutions (available from Dow Electronic Materials). Suitable alkaline conditioners include, but are not limited to: aqueous alkaline surfactant solutions containing one or more quaternary amines and polyamines Examples of commercially available alkaline surfactants are CIRCUPOSITTM Conditioner 231, 3325, 3323A, 813 and 860 formulations. Optionally, the substrate and through-holes are rinsed with water.
  • Micro-etching is designed to provide a micro-roughened metal surface on exposed metal (e.g. innerlayers and surface etch) to enhance subsequent adhesion of plated electroless metal and later electroplate.
  • Micro-etches include, but are not limited to 60 g/L to 120 g/L sodium persulfate or sodium or potassium oxymonopersulfate and sulfuric acid (2%) mixture, or generic sulfuric acid/hydrogen peroxide.
  • Examples of commercially available micro-etching compositions are CIRCUPOSITTM Microetch 3330 Etch solution and PREPOSITTM 748 Etch solution (available from Dow Electronic Materials).
  • the substrate is rinsed with water.
  • a pre-dip may then applied to the micro-etched substrate and through-holes.
  • Pre-dips include, but are not limited to organic salts such as sodium potassium tartrate or sodium citrate, 0.5% to 3% sulfuric acid or an acidic solution of 25 g/L to 75 g/L sodium chloride.
  • a catalyst may then be applied to the substrate.
  • Conventional catalysts may be used such as conventional tin/palladium colloidal catalysts.
  • Commercially available catalysts include, but are not limited to CATAPOSITTM 44 and CATAPOSITTM 404 catalyst formulations (available from Dow Electronic Materials).
  • Application may be done by conventional methods used in the art, such as immersing the substrate in a solution of the catalyst or by spraying or by atomization using conventional apparatus.
  • Catalyst dwell time may range from 1 minute to 10 minutes, typically from 2 minutes to 8 minutes for vertical equipment and for 25 seconds to 120 seconds for horizontal equipment.
  • the catalysts may be applied at temperatures from room temperature to 80° C., typically from 30° C. to 60° C.
  • the substrate and through-holes optionally may be rinsed with water after application of the catalyst.
  • the substrate and walls of the through-holes are then electrolessly plated with metal using the electroless metal composition.
  • Plating times and temperatures may be conventional. Typically metal deposition may be done at temperatures of 20° C. to 80° C., more typically from 30° C. to 60° C.
  • the substrate may be immersed in the electroless plating composition or the electroless composition may be sprayed onto the substrate. Typically, electroless plating may be done for 5 seconds to 30 minutes; however, plating times may vary depending on the thickness of the metal desired.
  • anti-tarnish may be applied to the metal.
  • Conventional anti-tarnish compositions may be used.
  • An example of anti-tarnish is ANTI TARNISHTM 7130 solution (available from Dow Electronic Materials).
  • the substrate may optionally be rinsed with water and then the boards may be dried.
  • the substrates may undergo further processing.
  • Further processing may include conventional processing by photoimaging and further metal deposition on the substrates such as electrolytic metal deposition of, for example, copper, copper alloys, tin and tin alloys.
  • the combination of the one or more tertiary amines and glyoxylic acid, salts or mixtures thereof provide a stable electroless metal plating composition which is formaldehyde-free and environmentally friendly.
  • the tertiary amines inhibit the decomposition of glyoxylic acids and its salts, thus prolonging the life of the plating composition and reducing the cost of the operation of the plating composition as replacement with glyoxylic acid or its salts is reduced or eliminated.
  • the combination of the one or more tertiary amines, salts, halides or mixtures thereof and the glyoxylic acid, salts or mixtures thereof at the molar ratios provides for a more efficient electroless metal plating process than many conventional electroless metal compositions and plating processes.
  • the plating compositions may provide for substantially uniform, bright metal deposits on substrates and reduced skip plating.
  • Glyoxylic acid-reduced electroless copper plating compositions were prepared as shown below.
  • the compositions included copper ions, glyoxylic acid as reducing agent, potassium tartrate as copper complexing agent, potassium hydroxide as pH adjusting agent, suppressors of glyoxylic acid decomposition, and 2,2′-dipyridyl as stabilizer.
  • the electroless copper compositions were free of formaldehyde. They were tested for the quality of their copper deposits and the stability of the glyoxylic acid.
  • the temperature of the composition of Formulation 1 of Table 1 was maintained at 40° C. and the pH of the composition was 13 during electroless copper deposition. Copper was deposited on substrates for 5 minutes.
  • the substrates used were unclad S1141 epoxy/glass laminates with dimensions 5 cm ⁇ 5 cm and copper-clad S1141 epoxy/glass multi-laminate boards (six layers) with dimensions 2 cm ⁇ 3.5 cm obtained from Shengyi Technology Co., Ltd.
  • the former were used for measuring the deposition rate, and the latter were used for evaluating the backlight performance of the through-holes.
  • the drill smear and other impurities of the through-holes in each board were then removed in a vertical desmear line process as follows:
  • the boards were treated with solvent swell composed of 12.5% CIRCUPOSITTM MLB CONDITIONER 211 solution for 5 minutes at 75° C. 2. Each board was then rinsed with cold water for 3 minutes. 3. The boards were then treated with an alkaline promoter of aqueous alkaline permanganate composed of 10% CIRCUPOSITTM MLB PROMOTER 213-A solution for 10 minutes at 80° C. 4. Each board was then rinsed with cold water for 3 minutes. 5. The boards were then treated with an aqueous neutralizer composed of 5% CIRCUPOSITTM MLB NEUTRALIZER 216-5 solution for 5 minutes at 40° C. 6. Each board was then rinsed with cold water for 3 minutes. 7.
  • each board/laminate was immersed in an aqueous bath containing 3% CIRCUPOSITTM CONDITIONER 3323A solution for 5 minutes at 40° C. 8. Each board/laminate was then rinsed with cold water for 4 minutes. 9. The through-holes of each board were then microetched with an aqueous acidic solution of 100 g/L sodium persulfate and 2% v/v sulfuric acid at room temperature for 1 minute. 10. Each board was then rinsed with cold water for 3 minutes. 11. A pre-dip was then applied to each board/laminate for 1 minute at room temperature. The pre-dip was CATAPREPTM 404 solution obtained from Rohm and Haas Electronic Materials. 12.
  • the boards/laminates were then primed for 5 minutes at 40° C. with a catalyst bath for electroless copper metallization.
  • the catalyst bath contained 2% CATAPOSITTM 44 solution, which was obtained from Rohm and Haas Electronic Materials. 13.
  • the boards/laminates were then rinsed with cold water for 2 minutes. 14.
  • the boards/laminates were then activated with 2.5% ACCELERATORTM 19E solution at room temperature for 2 minutes. 15.
  • the boards/laminates were then rinsed with cold water for 2 minutes. 16.
  • Each board/laminate was then immersed in the electroless copper plating composition of Formulation 1 for electroless copper deposition.
  • the copper deposition was done for 5 minutes at 40° C. at a pH of 13. 17.
  • Each copper plated board/laminate was then rinsed with cold water for 2 minutes. 18. Each copper plated board/laminate was then rinsed with deionised water for 1 minute. 19. After blow-drying, each laminates was observed for the quality of copper deposits, and the deposition rate was then measured by a wet titration method. 20.
  • Each board was then sectioned laterally to expose the copper plated walls of the through-holes. Multiple lateral sections 1 mm thick were taken from the walls of the sectioned through-holes of each board to determine the through-hole wall coverage for the boards using the conventional European Backlight Grading Scale from 0 to 5, where 0 means the worst results and 5 the best results. Reference samples showing results from 0 to 5 are shown in the FIGURE.
  • Each lateral section was placed under a conventional optical microscope of 50 ⁇ magnification with a light source. The light was applied to the backside of the sample. If no light was observed, the sample was completely copper plated and the image under the microscope was black as shown in reference sample marked 5.0 of the FIGURE. If some light was observed, the lateral section was compared to the reference samples marked 0.0 to 4.5. The more light which passed through the sample the lower the backlight rating and the poorer the plating quality.
  • the S1141 copper plated boards had average backlight values of 4.0 which was an acceptable value for commercial backlight values.
  • glyoxylic acid concentrations were determined by a wet titration method. The bath solution mentioned above was idled at 40° C. with air agitation. The glyoxylic acid concentrations were then measured after 6 hours and the percentage of remaining glyoxylic acid in the bath was calculated. The following method was used to calculate the glyoxylic acid concentrations:
  • the copper deposits obtained from the bath composition of Formulation 1 were salmon pink. Minor amounts of skip plating were observed. The deposition rate measured was 0.19 ⁇ m/5 minutes.
  • Formulations 2 to 4 of Table 1 were processed in the same way as Example 1.
  • the temperature of the compositions was maintained at 40° C. and a pH of 13 during electroless copper deposition. Copper was deposited on substrates for 5 minutes.
  • N,N,N′,N′-tetrakis(2-hydroxypropyl)ethylenediamine was used to suppress the glyoxylic acid decomposition.
  • the results showed that the copper deposits were red and smooth and no skip plating was observed.
  • the deposition rate was 0.32 ⁇ m/5 min.
  • the S1141 copper plated boards had average backlight values of 3.5. After 6 hours idling, there was still 65% glyoxylic acid left, and no copper oxide was observed. Thus the electroless copper composition was stable.
  • Formulations 5 and 6 of Table 2 were blank controls of formaldehyde and glyoxylic acid as reducing agents for copper. No reducing agent decomposition suppressors were added into the bath solutions. The temperature of the solutions was maintained at 40° C. and a pH of 13 during the idling test with air agitation. After 6 hours about 69% of the formaldehyde remained, and no copper oxide was observed. This suggested the electroless copper composition was stable, and decomposition of formaldehyde by the Cannizzaro reaction was not a serious issue.
  • Formulation 6 which included glyoxylic acid only had 20% glyoxylic acid left after 6 hours idling.
  • the decomposition rate of glyoxylic acid was very rapid such that from a practical production point of view, glyoxylic acid would not be a suitable substitute for formaldehyde.
  • the rapid decomposition of glyoxylic acid would result in sudden termination of electroless plating and high cost for replenishing the reducing agent. This is one of the main barriers for application of glyoxylic acid as a reducing agent in electroless copper plating solutions.
  • Formulations 7 and 8 included two conventional Cannizzaro reaction-suppressing agents, potassium stannate and hexamethylenediamine, respectively. Their molar concentrations were around 0.02 M. The temperature of the solutions was maintained at 40° C. and a pH of 13 during the idling test with air agitation. After 6 hours of idling, only about 20% glyoxylic acid remained in each solution. This is substantially the same as the electroless copper plating solution of Formulation 6 where no Cannizzaro reaction-suppressing agent was added. The conventional Cannizzaro reaction-suppressing agents, potassium stannate and hexamethylenediamine, did not effectively suppress glyoxylic acid decomposition.
  • succinic acid another conventional Cannizzaro reaction-suppressing agent was tested.
  • the temperature of the composition was maintained at 40° C. with a pH of 13 during the idling test with air agitation. After 6 hours, only around 20% glyoxylic acid remained.
  • the succinic acid did not effectively suppress the Cannizzaro reaction.
  • Formulations 10 and 11 included triethylamine and N,N,N′,N′-tetramethylethylenediamine, respectively, as suppressors of glyoxylic acid decomposition. Both are tertiary amines; however, none of the alkyl groups was substituted by functional groups, such as carboxylic acid, carboxylate, hydroxyl or phosphonic acid.
  • the temperature of the composition was maintained at 40° C. with a pH of 13 during the idling test with air agitation. After 6 hours idling time only around 21% glyoxylic acid remained. This was substantially the same as the control solution of Formulation 6 in Example 4 which had 20% remaining. The two unsubstituted tertiary amines did not show acceptable glyoxylic acid decomposition suppression.
  • a plurality of electroless copper plating solutions was prepared as shown in Table 5 below.
  • the glyoxylic acid decomposition suppressor was triisopropanolamine.
  • the molar ratio of the triisopropanolamine to glyoxylic acid was varied with the remainder of the components kept at the same concentration in the eleven formulations.
  • Example 7 The electroless copper plating solutions of Example 7 were tested for their plating performance and stability.
  • the substrates used were of the same type as in Example 2 above.
  • the substrates were treated and electroless plated as described in Example 2.
  • the temperature of the plating solutions was maintained at 40° C. with a pH of 13 during electroless copper deposition. Copper was deposited on the substrates for 5 minutes. The results are shown in Table 9.
  • a plurality of electroless copper plating solutions was prepared as shown in Table 10 below.
  • the glyoxylic acid decomposition suppressor was triisopropanolamine.
  • the molar ratio of the triisopropanolamine to glyoxylic acid was varied with the remainder of the components kept at the same concentration in the nine formulations.
  • the temperature of the plating solutions was maintained at 40° C. with a pH of 13 and air agitation.
  • the remaining glyoxylic acid was measured after 6 hours idling. The results are shown in Table 11.
  • the plating solutions with a molar ratio of TIPA:GA as low as 0.05:1 started showing a suppressing effect on the decomposition of glyoxylic acid.
  • the concentration of the suppressor By increasing the concentration of the suppressor, remaining glyoxylic acid gradually increased from 19% where there was no triisopropanolamine in the plating solution to 61% where the ratio of TIPA:GA was 1.6:1. Beyond the molar ratio of 1.6:1, the suppressing capability of the triisopropanolamine tended to stability as shown by the results obtained in Formulations 13-8 and 13-9.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microelectronics & Electronic Packaging (AREA)
  • Manufacturing & Machinery (AREA)
  • Inorganic Chemistry (AREA)
  • Chemically Coating (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Electrochemistry (AREA)
  • Manufacturing Of Printed Wiring (AREA)
US14/552,478 2014-11-24 2014-11-24 Formaldehyde-free electroless metal plating compositions and methods Abandoned US20160145745A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
US14/552,478 US20160145745A1 (en) 2014-11-24 2014-11-24 Formaldehyde-free electroless metal plating compositions and methods
EP15193850.3A EP3023515A3 (en) 2014-11-24 2015-11-10 Formaldehyde-free electroless metal plating compositions and methods
TW104137388A TWI655319B (zh) 2014-11-24 2015-11-12 無甲醛無電極金屬鍍敷組合物及方法
JP2015224151A JP6138892B2 (ja) 2014-11-24 2015-11-16 ホルムアルデヒド不含無電解金属メッキ組成物及び方法
KR1020150163009A KR101739421B1 (ko) 2014-11-24 2015-11-20 포름알데하이드-부재 무전해 금속 도금 조성물 및 방법
CN201510809868.0A CN105624653B (zh) 2014-11-24 2015-11-20 无甲醛无电极金属镀敷组合物和方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US14/552,478 US20160145745A1 (en) 2014-11-24 2014-11-24 Formaldehyde-free electroless metal plating compositions and methods

Publications (1)

Publication Number Publication Date
US20160145745A1 true US20160145745A1 (en) 2016-05-26

Family

ID=54834611

Family Applications (1)

Application Number Title Priority Date Filing Date
US14/552,478 Abandoned US20160145745A1 (en) 2014-11-24 2014-11-24 Formaldehyde-free electroless metal plating compositions and methods

Country Status (6)

Country Link
US (1) US20160145745A1 (ja)
EP (1) EP3023515A3 (ja)
JP (1) JP6138892B2 (ja)
KR (1) KR101739421B1 (ja)
CN (1) CN105624653B (ja)
TW (1) TWI655319B (ja)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3578683A1 (en) * 2018-06-08 2019-12-11 ATOTECH Deutschland GmbH Electroless copper or copper alloy plating bath and method for plating
WO2020234158A1 (en) * 2019-05-17 2020-11-26 Fundación Cidetec Electroless metal coatings exhibiting wave permeability and method for the manufacture thereof
WO2020234162A1 (en) * 2019-05-17 2020-11-26 Fundación Cidetec Light permeable metallic coatings and method for the manufacture thereof
CN113549964A (zh) * 2021-07-28 2021-10-26 重庆立道新材料科技有限公司 一种无氰镀铜锌合金晶粒细化剂及其应用
US20210371998A1 (en) * 2020-05-27 2021-12-02 Macdermid Enthone Inc. Gold Plating Bath and Gold Plated Final Finish

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2736845C2 (ru) * 2016-06-09 2020-11-20 Басф Се Строительные химические композиции, включающие бисульфитный аддукт глиоксиловой кислоты
CN107829116B (zh) * 2017-12-14 2019-08-09 广州三孚新材料科技股份有限公司 无氰碱性镀铜电镀液
EP4234758A1 (en) * 2020-10-21 2023-08-30 Asahi Kasei Kabushiki Kaisha Method for manufacturing conductive pattern-provided structure

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4617205A (en) * 1984-12-21 1986-10-14 Omi International Corporation Formaldehyde-free autocatalytic electroless copper plating
JP3227504B2 (ja) * 1993-04-19 2001-11-12 奥野製薬工業株式会社 無電解銅めっき液
US20020064592A1 (en) * 2000-11-29 2002-05-30 Madhav Datta Electroless method of seed layer depostion, repair, and fabrication of Cu interconnects
JP4482744B2 (ja) 2001-02-23 2010-06-16 株式会社日立製作所 無電解銅めっき液、無電解銅めっき方法、配線板の製造方法
JP2003147541A (ja) 2001-11-15 2003-05-21 Hitachi Ltd 無電解銅めっき液、無電解銅めっき用補給液及び配線板の製造方法
US6897152B2 (en) * 2003-02-05 2005-05-24 Enthone Inc. Copper bath composition for electroless and/or electrolytic filling of vias and trenches for integrated circuit fabrication
TW200813255A (en) * 2006-07-07 2008-03-16 Rohm & Haas Elect Mat Environmentally friendly electroless copper compositions
US7968455B2 (en) * 2006-10-17 2011-06-28 Enthone Inc. Copper deposition for filling features in manufacture of microelectronic devices
JP5588597B2 (ja) * 2007-03-23 2014-09-10 富士フイルム株式会社 導電性材料の製造方法及び製造装置
JP5525762B2 (ja) * 2008-07-01 2014-06-18 上村工業株式会社 無電解めっき液及びそれを用いた無電解めっき方法、並びに配線基板の製造方法
JP2012174758A (ja) * 2011-02-18 2012-09-10 Fujifilm Corp 多層基板の製造方法、デスミア処理方法
US20140242264A1 (en) * 2011-10-05 2014-08-28 Atotech Deutschland Gmbh Formaldehyde-free electroless copper plating solution
EP2784181B1 (en) * 2013-03-27 2015-12-09 ATOTECH Deutschland GmbH Electroless copper plating solution
CN105008587B (zh) * 2013-03-27 2018-04-17 埃托特克德国有限公司 化学镀铜溶液

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3578683A1 (en) * 2018-06-08 2019-12-11 ATOTECH Deutschland GmbH Electroless copper or copper alloy plating bath and method for plating
WO2019234085A1 (en) * 2018-06-08 2019-12-12 Atotech Deutschland Gmbh Electroless copper or copper alloy plating bath and method for plating
US11396706B2 (en) 2018-06-08 2022-07-26 Atotech Deutschland Gmbh Electroless copper or copper alloy plating bath and method for plating
WO2020234158A1 (en) * 2019-05-17 2020-11-26 Fundación Cidetec Electroless metal coatings exhibiting wave permeability and method for the manufacture thereof
WO2020234162A1 (en) * 2019-05-17 2020-11-26 Fundación Cidetec Light permeable metallic coatings and method for the manufacture thereof
US20220235467A1 (en) * 2019-05-17 2022-07-28 Fundación Cidetec Electroless metal coatings exhibiting wave permeability and method for the manufacture thereof
US20210371998A1 (en) * 2020-05-27 2021-12-02 Macdermid Enthone Inc. Gold Plating Bath and Gold Plated Final Finish
CN115516133A (zh) * 2020-05-27 2022-12-23 麦克德米德乐思公司 镀金浴和镀金最终饰面
CN113549964A (zh) * 2021-07-28 2021-10-26 重庆立道新材料科技有限公司 一种无氰镀铜锌合金晶粒细化剂及其应用

Also Published As

Publication number Publication date
CN105624653A (zh) 2016-06-01
JP2016128604A (ja) 2016-07-14
TW201621084A (zh) 2016-06-16
KR20160061889A (ko) 2016-06-01
TWI655319B (zh) 2019-04-01
CN105624653B (zh) 2019-03-15
JP6138892B2 (ja) 2017-05-31
EP3023515A2 (en) 2016-05-25
EP3023515A3 (en) 2016-07-27
KR101739421B1 (ko) 2017-05-24

Similar Documents

Publication Publication Date Title
US20160145745A1 (en) Formaldehyde-free electroless metal plating compositions and methods
US9702046B2 (en) Electroless copper plating compositions
KR102060983B1 (ko) 무전해 구리 도금 조성물
KR101953940B1 (ko) 무전해 구리 도금 수용액
CN110607521B (zh) 无电镀铜组合物和用于在基材上无电镀铜的方法
US9809883B2 (en) Formaldehyde free electroless copper plating compositions and methods
JP6814845B2 (ja) 無電解銅めっき用組成物および基材上に銅を無電解めっきするための方法
JP2019218629A (ja) 無電解銅めっき用組成物および基材上に銅を無電解めっきするための方法
US11512394B2 (en) Electroless gold plating bath

Legal Events

Date Code Title Description
AS Assignment

Owner name: ROHM AND HAAS ELECRONIC MATERIALS LLC, MASSACHUSET

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:WU, WEIGANG;LI, CRYSTAL P.L.;LIANG, ZHIXIONG;REEL/FRAME:035413/0135

Effective date: 20141126

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION