US2707166A - Electrodeposition of copper from an acid bath - Google Patents

Electrodeposition of copper from an acid bath Download PDF

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Publication number
US2707166A
US2707166A US290091A US29009152A US2707166A US 2707166 A US2707166 A US 2707166A US 290091 A US290091 A US 290091A US 29009152 A US29009152 A US 29009152A US 2707166 A US2707166 A US 2707166A
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United States
Prior art keywords
copper
group
liter
sulfate
bath
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
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US290091A
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English (en)
Inventor
Brown Henry
Richard A Fellows
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Udylite Corp
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Udylite Corp
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Publication date
Priority to NL83873D priority Critical patent/NL83873C/xx
Priority to NLAANVRAGE7804190,A priority patent/NL178453B/xx
Priority to BE520209D priority patent/BE520209A/xx
Application filed by Udylite Corp filed Critical Udylite Corp
Priority to US290091A priority patent/US2707166A/en
Priority to GB13949/53A priority patent/GB736252A/en
Priority to FR1077492D priority patent/FR1077492A/fr
Priority to DEU2199A priority patent/DE947656C/de
Application granted granted Critical
Publication of US2707166A publication Critical patent/US2707166A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • 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

Definitions

  • This invention relates to the electrodeposition of copper from an aqueous acidic bath and more particularly concerns the utilization of selected addition agents to aqueous acidic baths for the purposes hereinafter stated.
  • the primary object of this invention is to decrease the grain size and increase the luster of the copper deposit without materially imparing the ductility of the plate or decreasing the current density range of the acidic copper plating bath.
  • R1 and R2 may be hydrogen, methyl or ethyl radicals
  • X is an anion selected from the group consisting of chloride, bromide, iodide, fluoride, sulfate, bisulfate and nitrate
  • Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, and phenyl and naphthyl radicals substituted with amino, alkyl substituted amino, hydroxy and alkoxy substituent groups.
  • the anion X is relatively unimportant and in addition to the anions above given may be any one of a wide variety of other anions, including organic anions such as formate, acetate, propionate, etc. It will be appreciated that the compounds represented by the above formula, when present in an acid copper bath, are highly ionized substances and the anion X is in ionic admixture with the other anions of the bath such as the sulfate anion, the nitrate anion, etc. It is believed that the diamino phenylphenazonium nucleus or ion is the dominant contributor to the beneficial effects of decreasing the grain size without materially impairing ductility of the plate which is obtained from the presence in the bath of any of the compounds of Formula A.
  • the phenyl or naphthyl radicals be substituted with amino or alkyl substituted amino groups, that the alkyl groups be either methyl or ethyl groups, and that the alkoxy group be methoxy or ethoxy; and for best bath life it is preferable to maintain a concentration of chloride, or its equivalent in bromide or iodide, of about .003 to about .020 gram/liter in the solution. It is to be understood that when X is either fluoride, sulfate, bisulfate or nitrate, that chloride, bromide or.
  • iodide ions in an amount equivalent to about .003to .020 gram/liter of chloride is preferably present in addition.
  • 2,707,166 Patented Apr. 26, 1955 contains a sutficient halide concentration, but it is usually preferable to replenish the halide during use in order to maintain the preferred minimum concentration of about .003 gram/liter of chloride or its equivalent.
  • Janus Green B is the dye commercially known as Janus Green B.
  • Janus Green B is sometimes designated Dia zine Green (Schultz #282) and chemically it may be designated briefly as diethyl-safranine-aZo-dimethyl-aniline.
  • Another preferred example which is not generally as commercially available as Janus Green B, is represented by the above formula wherein R1 is hydrogen and R2 is a irfethyl radical, that is, dimethyl safranine azo dimethyl ani me.
  • the extremely useful addition agents represented by Formula A which efiectively accomplish the above stated object may, in general, be classified as the product of the coupling reaction of a diazotized amino phenazine with phenol, naphthol or aryl amino compounds including the alkyl substitution products of phenol, naphthol, or aryl amino compounds.
  • Janus Green B which is a diazotized amino phenazine coupled with dimethyl aniline, may be replaced by a diazotized amino phenazine coupled with other amino compounds such as substituted diethyl anilines and naphthylamines.
  • the total concentration of the mixed dye in the acidic aqueous bath preferably approximates the concentration of any component as indicated in Table 1.
  • Janus Green B may be mixed with Janus Black in a total concentration corresponding approximately to the concentration for either Janus Green B or Janus Black as given in Table 1.
  • concentrations of the dyes of Table 1 falling within the range of .005 to .04 gram/liter represent preferred quantities.
  • Janus Green B is commercially available in approximately 50% dye strength in admixture with an inorganic salt, but it is to be understood that the concentrations set forth herein and in the appended claims refer to dye strength.
  • composition of the acidic copper bath may vary over rather wide limits, although for the best grain refinement, rate of brightening and for the widest bright plating range, the following composition, designated Formula taining proportions of addition agents indicated in Table 1 include controlled temperatures, bath agitation and cathode current densities.
  • the bath temperatures may be from about 17 C. to 40 C. (approximately 70 F. to F.). Warmer temperatures above 40 C. tend to decrease the brightness of the plate, but temperatures up to 50 C. may be used satisfactorily.
  • Cathode agitation and preferably uniform air agitation is desirable.
  • dm. may be satisfactorily employed with the particular current density depending primarily upon the degree of agitation of the cathode film and the shape of the article to be plated.
  • an average cathode current density of 30-50 amps/sq. ft. may be used.
  • Formula B may include other ions for the purpose of increasing the conductivity of the solution such as sodium, potassium or ammonium ions. These ions are usually present in only minor concentrations.
  • the copper sulfate of Formula B may be replaced by copper nitrate in approximately equivalent proportions, and when acidified with small amounts of phosphoric acid, nitric acid or sulfuric acid, the beneficial effect of reducing the grain size and increasing the luster of the deposit by additions of small concentrations of compounds of the type shown in Table 1 is also evident.
  • the degree, however, of grain size, reduction and increase in luster is somewhat less extensive than is produced from the use of acidic baths made up primarily of copper sulfate.
  • the beneficial effect of reducing the grain size and increasing the luster of the deposit by additions of small concentrations of compounds of the type shown in Table 1 is also evident.
  • the degree, however, of grain size, reduction and increase in luster is somewhat less extensive than is produced from the use of acidic baths made up primarily of copper sulfate.
  • the copper sulfate of Formula B may be replaced by copper nitrate in approximately equivalent proportions, and when acidified with small amounts of phosphoric acid, n
  • copper sulfate or copper nitrate concentration in the bath may satisfactorily vary from as low as about 100 grams/liter up to saturation. Concentrations of acid above the equivalent in acidity of about 80-100 grams/ liter of sulfuric acid decrease the brightening effect of the addition agents represented by Formula A and are therefore to be avoided.
  • wetting agents may be advantageously present in the baths of this invention.
  • the surface-active compounds, sodium decyl sulfate and the sulfated mono-ethylene oxide condensate of decyl alcohol when present in small concentrations of about .01 to .06 gram/liter are effective in decreasing pitting and striation formation in the deposit due to the presence of harmful organic compounds or excessive concentrations of brighteners.
  • These wetting agents normally cause excessive frothing with air agitation, but in the presence of the addition agents of Table l, the frothing is minimized.
  • Example I CuSOaSHzQ 200 grams/liter. H2804 15 grams/liter. Janus Green B .003 gram/ liter. Temperature 70-95 F. Cathode current density 30-40 amps./ sq. ft.
  • Example II CuSO4.5HzO 200 grams/liter. H2804; 15 grams/liter. Janus Black .01 gram/liter. Temperatureun 7090 F. Cathode current density 30.40 amps./ sq. ft.
  • a bath for the electrodeposition of copper comprising an aqueous acidic solution of a material selected from the group consisting of copper sulfate and copper nitrate, and minor proportions of a compound having the structure:
  • R1 and R2 are radicals selected from the group consisting of hydrogen, methyl and ethyl radicals
  • X is an anion selected from the group consisting of chloride, bromide, iodide, fluoride, sulfate, bisulfate and nitrate
  • Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, and phenyl and naphthyl radicals substituted with amino, alkyl substituted ammo, hydroxy and alkoxy substituent groups.
  • a bath for the electrodeposition of copper in the form of a fine grain deposit comprising an aqueous acidic solution of a material selected from the group consisting of copper sulfate and copper nitrate and minor proportions of a compound selected from the group consisting of Janus Green, Janus Blue, Janus Black, Janus Gray, dimethyl safranine azo dimethyl aniline and mixtures thereof.
  • a bath for the electrodeposition of copper comprising an aqueous acidic solution of a material selected from the group consisting of copper sulfate and copper nitrate, and about .0015 to about .05 gram/liter of a compound having the structure:
  • R1 and R2 are radicals selected from the group consisting of hydrogen, methyl and ethyl radicals
  • X is an anion selected from the group consisting of chloride, bromide, iodide, fluoride, sulfate, bisulfate and nitrate
  • Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, and phenyl and naphthyl radicals substituted with amino, alkyl'substituted amino, hydroxy and alkoxy substituent groups.
  • a bath for the electrodeposition of copper in the form of a time grain deposit comprising an aqueous acidic ride, bromide, iodide, fluoride, sulfate,
  • a bath for the electrodeposition of copper comprising an aqueous acidic solution of a material selected from the group consisting of copper sulfate and copper nitrate and a minor proportion of Janus Green B.
  • a bath for the electrodeposition of copper comprisin g an aqueous acidic solution of a material selected from the group consisting of copper sulfate and copper nitrate and about .0015 to about .05 gram/liter of Janus Green B.
  • a bath for the electrodeposition of copper in the form of a fine grain deposit comprising an aqueous acidic solution of copper sulfate and .005 to .04 gram/ liter of Janus Green B.
  • aqueous acid copper solution containing a metal salt selected from the group consisting of copper sulfate and copper nitrate, said aqueous solution also containing minor proportions of a compound having the structure:
  • R1 and R2 are radicals selected from the group consisting of hydrogen, methyl and ethyl radicals
  • X is an anion selected from the group consisting of chloride, bromide, iodide, fluoride, sulfate, bisulfate and nitrate
  • Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, and phenyl and naphthyl radicals substituted with amino, alkyl substituted amino,
  • aqueous acidic copper solution containing a metal salt selected from the group consisting of copper sulfate and copper nitrate, said aqueous solution also containing minor proportions of a compound selected from a group consisting of Janus Green B, Janus Black, Janus Gray, Janus Blue, dimethylsafranine-azo-dimethyl-aniline and mixtures thereof.
  • aqueous acidic copper solution containing a metal salt selected from the group consisting of copper sulfate and copper nitrate, said aqueous solution also containing about .00l5 to about .05 grams/liter of a compound having the structure:
  • R1 and R2 are radicals selected from the group consisting of hydrogen, methyl and is an anion selected from the group consisting of chlobisulfate and nitrate, and Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, and phenyl and naphthyl radicals substituted with amino, alkyl substituted amino, hydroxy and alkoxy substituent groups.
  • a bath for the electrodeposition of copper comprising an aqueous acidic solution of a material selected from the group consisting of copper sulfate and copper nitrate, a halide selected from the group consisting of chloride, bromide and iodide in an amount equivalent ethyl radicals, X
  • R1 and R2 are radicals selected from the group consisting of hydrogen, methyl and ethyl radicals
  • X is an anion selected from the group consisting of chloride, bromide, iodide, fluoride, sulfate, bisulfate and nitrate
  • Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, phenyl and naphthyl radicals substituted with amino, and alkyl substituted amino, hydroxy and alkoxy substituent groups.
  • the step which comprises electrolyzing an aqueous acidic copper solution containing a metal salt selected from the group consisting of copper sulfate and copper nitrate, a halide selected from the group consisting of chloride, bromide and iodide in an amount equivalent to about .003 gram/ liter to about .020 gram/liter of chloride and a minor proportion of a compound having the structure wherein R1 and R2 are radicals selected from the group consisting of hydrogen, methyl and ethyl radicals, X is an anion selected from the group consisting of chloride, bromide, iodide, fluoride, sulfate, bisulfate and nitrate, and Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, and phenyl and naphthyl radicals substituted with amino, alkyl substituted amino, hydroxy and alkoxy substituent groups.
  • a metal salt selected from the group consisting of copper
  • a bath for the electrodeposition of copper comprising an aqueous acidic solution of a material selected from the group consisting of copper sulfate and copper nitrate, a halide selected from the group consisting of chloride, bromide and iodide in an amount equivalent to about .003 gram/liter to about .020 gram/liter of chloride, a minor proportion of a compound having the structure:
  • R1 and R2 are radicals selected from the group consisting of hydrogen, methyl and ethyl radicals
  • X is an anion selected from the group consisting of chloride, bromide, iodide, fluoride, sulfate, bisulfate and nitrate
  • Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, phenyl and naphthyl radicals substituted with amino, and alkyl substituted amino, hydroxy and alkoxy substituent groups, and a small amount of a wetting agent.
  • the step which comprises electrolyzing an aqueous acidic copper solution containing a metal salt selected from the group consisting of copper sulfate and copper nitrate, a halide selected from the group consisting of chloride, bromide and iodide in an amount equivalent to about .003 gram/- liter to about .020 gram/liter of chloride, a minor proportion of a compound having the structure:
  • R1 and R2 are radicals selected from the group consisting of hydrogen, methyl and ethyl radicals
  • X is an anion selected from the group consisting of chloride, bromide, iodide, fluoride, sulfate, bisulfate and nitrate
  • Z is an aromatic radical selected from the group consisting of phenyl, naphthyl, and phenyl and naphthyl radicals substituted with amino, alkyl substituted amino, hydroxy and alkoxy substituent groups and a small amount of a wetting agent.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electroplating And Plating Baths Therefor (AREA)
  • Electrolytic Production Of Metals (AREA)
US290091A 1952-05-26 1952-05-26 Electrodeposition of copper from an acid bath Expired - Lifetime US2707166A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
NL83873D NL83873C (de) 1952-05-26
NLAANVRAGE7804190,A NL178453B (nl) 1952-05-26 Werkwijze voor het elektrostatisch copieren.
BE520209D BE520209A (de) 1952-05-26
US290091A US2707166A (en) 1952-05-26 1952-05-26 Electrodeposition of copper from an acid bath
GB13949/53A GB736252A (en) 1952-05-26 1953-05-18 Improvements in electrodeposition of copper from an acid bath
FR1077492D FR1077492A (fr) 1952-05-26 1953-05-21 Perfectionnements au dépôt électrolytique de cuivre à partir d'un bain acide
DEU2199A DE947656C (de) 1952-05-26 1953-05-23 Bad zur galvanischen Herstellung von Kupferueberzuegen

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US290091A US2707166A (en) 1952-05-26 1952-05-26 Electrodeposition of copper from an acid bath

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US (1) US2707166A (de)
BE (1) BE520209A (de)
DE (1) DE947656C (de)
FR (1) FR1077492A (de)
GB (1) GB736252A (de)
NL (2) NL178453B (de)

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2738318A (en) * 1954-12-28 1956-03-13 Udylite Res Corp Electrodeposition of copper from an acid bath
US2842488A (en) * 1954-11-05 1958-07-08 Dehydag Gmbh Process for the production of metal electrodeposits
US2882209A (en) * 1957-05-20 1959-04-14 Udylite Res Corp Electrodeposition of copper from an acid bath
US3267010A (en) * 1962-04-16 1966-08-16 Udylite Corp Electrodeposition of copper from acidic baths
US3288690A (en) * 1962-04-16 1966-11-29 Udylite Corp Electrodeposition of copper from acidic baths
US3328273A (en) * 1966-08-15 1967-06-27 Udylite Corp Electro-deposition of copper from acidic baths
US3743584A (en) * 1970-06-06 1973-07-03 Schering Ag Acid bright copper plating bath
US4316778A (en) * 1980-09-24 1982-02-23 Rca Corporation Method for the manufacture of recording substrates for capacitance electronic discs
US4376685A (en) * 1981-06-24 1983-03-15 M&T Chemicals Inc. Acid copper electroplating baths containing brightening and leveling additives
US4469564A (en) * 1982-08-11 1984-09-04 At&T Bell Laboratories Copper electroplating process
DE3420999A1 (de) * 1983-06-10 1984-12-13 Omi International Corp., Warren, Mich. Waessriges saures galvanisches kupferbad und verfahren zur galvanischen abscheidung eines glaenzenden eingeebneten kupferueberzugs auf einem leitfaehigen substrat aus diesem bad
US4551212A (en) * 1985-03-11 1985-11-05 Rca Corporation Bath and process for the electrodeposition of micromachinable copper and additive for said bath
US6709568B2 (en) 2002-06-13 2004-03-23 Advanced Technology Materials, Inc. Method for determining concentrations of additives in acid copper electrochemical deposition baths
US20050067304A1 (en) * 2003-09-26 2005-03-31 King Mackenzie E. Electrode assembly for analysis of metal electroplating solution, comprising self-cleaning mechanism, plating optimization mechanism, and/or voltage limiting mechanism
US20050109624A1 (en) * 2003-11-25 2005-05-26 Mackenzie King On-wafer electrochemical deposition plating metrology process and apparatus
US20050194248A1 (en) * 1999-04-13 2005-09-08 Hanson Kyle M. Apparatus and methods for electrochemical processing of microelectronic workpieces
US20050224370A1 (en) * 2004-04-07 2005-10-13 Jun Liu Electrochemical deposition analysis system including high-stability electrode
US20050247576A1 (en) * 2004-05-04 2005-11-10 Tom Glenn M Electrochemical drive circuitry and method
US20060102475A1 (en) * 2004-04-27 2006-05-18 Jianwen Han Methods and apparatus for determining organic component concentrations in an electrolytic solution
US20060266648A1 (en) * 2002-12-17 2006-11-30 King Mackenzie E Process analyzer for monitoring electrochemical deposition solutions
US20070108062A1 (en) * 2003-11-19 2007-05-17 Atotech Deutschland Gmbh Acidic bath for electrolytically depositing a copper deposit containing halogenated or pseudohalogenated monomeric phenazinium compounds
US7435320B2 (en) 2004-04-30 2008-10-14 Advanced Technology Materials, Inc. Methods and apparatuses for monitoring organic additives in electrochemical deposition solutions
US7438788B2 (en) 1999-04-13 2008-10-21 Semitool, Inc. Apparatus and methods for electrochemical processing of microelectronic workpieces
US7872130B2 (en) 2002-12-20 2011-01-18 Atotech Deutschland Gmbh Mixture of oligomeric phenazinium compounds and acid bath for electrolytically depositing a copper deposit
US10982343B2 (en) 2017-11-09 2021-04-20 Atotech Deutschland Gmbh Plating compositions for electrolytic copper deposition, its use and a method for electrolytically depositing a copper or copper alloy layer onto at least one surface of a substrate
US11174566B2 (en) 2017-06-16 2021-11-16 Atotech Deutschland Gmbh Aqueous acidic copper electroplating bath and method for electrolytically depositing of a copper coating

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102005011708B3 (de) 2005-03-11 2007-03-01 Atotech Deutschland Gmbh Polyvinylammoniumverbindung und Verfahren zu deren Herstellung sowie diese Verbindung enthaltende saure Lösung und Verfahren zum elektrolytischen Abscheiden eines Kupferniederschlages

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2291590A (en) * 1940-03-11 1942-07-28 Harshaw Chem Corp Electrodeposition of metals
US2326999A (en) * 1940-03-11 1943-08-17 Harshaw Chem Corp Nickel plating
US2602774A (en) * 1948-05-11 1952-07-08 John F Beaver Method of plating copper

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2489538A (en) * 1941-05-24 1949-11-29 Gen Motors Corp Electrodeposition of copper
US2563360A (en) * 1941-05-24 1951-08-07 Gen Motors Corp Electrodeposition of copper

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2291590A (en) * 1940-03-11 1942-07-28 Harshaw Chem Corp Electrodeposition of metals
US2326999A (en) * 1940-03-11 1943-08-17 Harshaw Chem Corp Nickel plating
US2602774A (en) * 1948-05-11 1952-07-08 John F Beaver Method of plating copper

Cited By (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2842488A (en) * 1954-11-05 1958-07-08 Dehydag Gmbh Process for the production of metal electrodeposits
US2905602A (en) * 1954-11-05 1959-09-22 Dehydag Gmbh Production of metal electrodeposits
US2738318A (en) * 1954-12-28 1956-03-13 Udylite Res Corp Electrodeposition of copper from an acid bath
US2882209A (en) * 1957-05-20 1959-04-14 Udylite Res Corp Electrodeposition of copper from an acid bath
US3267010A (en) * 1962-04-16 1966-08-16 Udylite Corp Electrodeposition of copper from acidic baths
US3288690A (en) * 1962-04-16 1966-11-29 Udylite Corp Electrodeposition of copper from acidic baths
US3328273A (en) * 1966-08-15 1967-06-27 Udylite Corp Electro-deposition of copper from acidic baths
US3743584A (en) * 1970-06-06 1973-07-03 Schering Ag Acid bright copper plating bath
US4316778A (en) * 1980-09-24 1982-02-23 Rca Corporation Method for the manufacture of recording substrates for capacitance electronic discs
US4376685A (en) * 1981-06-24 1983-03-15 M&T Chemicals Inc. Acid copper electroplating baths containing brightening and leveling additives
US4469564A (en) * 1982-08-11 1984-09-04 At&T Bell Laboratories Copper electroplating process
DE3420999A1 (de) * 1983-06-10 1984-12-13 Omi International Corp., Warren, Mich. Waessriges saures galvanisches kupferbad und verfahren zur galvanischen abscheidung eines glaenzenden eingeebneten kupferueberzugs auf einem leitfaehigen substrat aus diesem bad
US4551212A (en) * 1985-03-11 1985-11-05 Rca Corporation Bath and process for the electrodeposition of micromachinable copper and additive for said bath
US20050194248A1 (en) * 1999-04-13 2005-09-08 Hanson Kyle M. Apparatus and methods for electrochemical processing of microelectronic workpieces
US7438788B2 (en) 1999-04-13 2008-10-21 Semitool, Inc. Apparatus and methods for electrochemical processing of microelectronic workpieces
US20080217167A9 (en) * 1999-04-13 2008-09-11 Hanson Kyle M Apparatus and methods for electrochemical processing of microelectronic workpieces
US7264698B2 (en) 1999-04-13 2007-09-04 Semitool, Inc. Apparatus and methods for electrochemical processing of microelectronic workpieces
US6709568B2 (en) 2002-06-13 2004-03-23 Advanced Technology Materials, Inc. Method for determining concentrations of additives in acid copper electrochemical deposition baths
US20060266648A1 (en) * 2002-12-17 2006-11-30 King Mackenzie E Process analyzer for monitoring electrochemical deposition solutions
US7872130B2 (en) 2002-12-20 2011-01-18 Atotech Deutschland Gmbh Mixture of oligomeric phenazinium compounds and acid bath for electrolytically depositing a copper deposit
US20050067304A1 (en) * 2003-09-26 2005-03-31 King Mackenzie E. Electrode assembly for analysis of metal electroplating solution, comprising self-cleaning mechanism, plating optimization mechanism, and/or voltage limiting mechanism
US20070108062A1 (en) * 2003-11-19 2007-05-17 Atotech Deutschland Gmbh Acidic bath for electrolytically depositing a copper deposit containing halogenated or pseudohalogenated monomeric phenazinium compounds
US7786303B2 (en) 2003-11-19 2010-08-31 Atotech Deutschland Gmbh Acidic bath for electrolytically depositing a copper deposit containing halogenated or pseudohalogenated monomeric phenazinium compounds
US20050109624A1 (en) * 2003-11-25 2005-05-26 Mackenzie King On-wafer electrochemical deposition plating metrology process and apparatus
US20050224370A1 (en) * 2004-04-07 2005-10-13 Jun Liu Electrochemical deposition analysis system including high-stability electrode
US20060102475A1 (en) * 2004-04-27 2006-05-18 Jianwen Han Methods and apparatus for determining organic component concentrations in an electrolytic solution
US7427344B2 (en) 2004-04-27 2008-09-23 Advanced Technology Materials, Inc. Methods for determining organic component concentrations in an electrolytic solution
US7435320B2 (en) 2004-04-30 2008-10-14 Advanced Technology Materials, Inc. Methods and apparatuses for monitoring organic additives in electrochemical deposition solutions
US7427346B2 (en) 2004-05-04 2008-09-23 Advanced Technology Materials, Inc. Electrochemical drive circuitry and method
US20050247576A1 (en) * 2004-05-04 2005-11-10 Tom Glenn M Electrochemical drive circuitry and method
US11174566B2 (en) 2017-06-16 2021-11-16 Atotech Deutschland Gmbh Aqueous acidic copper electroplating bath and method for electrolytically depositing of a copper coating
US10982343B2 (en) 2017-11-09 2021-04-20 Atotech Deutschland Gmbh Plating compositions for electrolytic copper deposition, its use and a method for electrolytically depositing a copper or copper alloy layer onto at least one surface of a substrate

Also Published As

Publication number Publication date
DE947656C (de) 1956-08-23
GB736252A (en) 1955-09-07
NL178453B (nl)
BE520209A (de)
FR1077492A (fr) 1954-11-08
NL83873C (de)

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