US20030010646A1 - Electrolytic copper plating solutions - Google Patents
Electrolytic copper plating solutions Download PDFInfo
- Publication number
- US20030010646A1 US20030010646A1 US10/225,677 US22567702A US2003010646A1 US 20030010646 A1 US20030010646 A1 US 20030010646A1 US 22567702 A US22567702 A US 22567702A US 2003010646 A1 US2003010646 A1 US 2003010646A1
- Authority
- US
- United States
- Prior art keywords
- composition
- brightener
- electroplating
- copper
- concentration
- 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
Links
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 59
- 239000010949 copper Substances 0.000 title claims abstract description 59
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 58
- 238000007747 plating Methods 0.000 title claims description 87
- 239000000203 mixture Substances 0.000 claims abstract description 59
- 238000009713 electroplating Methods 0.000 claims abstract description 47
- 238000000034 method Methods 0.000 claims abstract description 39
- 239000003795 chemical substances by application Substances 0.000 claims description 31
- 239000000758 substrate Substances 0.000 claims description 23
- 150000001879 copper Chemical class 0.000 claims description 12
- 239000004065 semiconductor Substances 0.000 claims description 12
- 150000001875 compounds Chemical class 0.000 claims description 11
- 239000003792 electrolyte Substances 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 230000002378 acidificating effect Effects 0.000 claims description 6
- 238000000151 deposition Methods 0.000 claims description 5
- 125000000547 substituted alkyl group Chemical group 0.000 claims description 5
- 125000004404 heteroalkyl group Chemical group 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- 125000004434 sulfur atom Chemical group 0.000 claims description 4
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims description 3
- 229920000570 polyether Polymers 0.000 claims description 3
- 239000000126 substance Chemical group 0.000 claims description 3
- 125000003107 substituted aryl group Chemical group 0.000 claims description 3
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims description 2
- 125000001072 heteroaryl group Chemical group 0.000 claims description 2
- 125000000542 sulfonic acid group Chemical group 0.000 claims description 2
- 239000004721 Polyphenylene oxide Substances 0.000 claims 1
- 239000000243 solution Substances 0.000 description 34
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 15
- -1 copper sulfate) Chemical class 0.000 description 15
- 125000003118 aryl group Chemical group 0.000 description 9
- 230000007547 defect Effects 0.000 description 9
- 125000000217 alkyl group Chemical group 0.000 description 8
- 239000002253 acid Substances 0.000 description 6
- 150000001412 amines Chemical class 0.000 description 5
- 125000004432 carbon atom Chemical group C* 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 239000004094 surface-active agent Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 4
- 229920001577 copolymer Polymers 0.000 description 4
- 230000008021 deposition Effects 0.000 description 4
- 238000010884 ion-beam technique Methods 0.000 description 4
- DNIAPMSPPWPWGF-UHFFFAOYSA-N monopropylene glycol Natural products CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 4
- 238000001020 plasma etching Methods 0.000 description 4
- 229920001223 polyethylene glycol Polymers 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical compound CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- 229910016374 CuSO45H2O Inorganic materials 0.000 description 3
- 239000002202 Polyethylene glycol Substances 0.000 description 3
- 229910006127 SO3X Inorganic materials 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 description 3
- 238000004100 electronic packaging Methods 0.000 description 3
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 125000001624 naphthyl group Chemical group 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- 125000004433 nitrogen atom Chemical group N* 0.000 description 3
- 125000001424 substituent group Chemical group 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- AFEITPOSEVENMK-UHFFFAOYSA-N 1-(2-hydroxyethyl)imidazolidine-2-thione Chemical compound OCCN1CCNC1=S AFEITPOSEVENMK-UHFFFAOYSA-N 0.000 description 2
- OBDVFOBWBHMJDG-UHFFFAOYSA-N 3-mercapto-1-propanesulfonic acid Chemical compound OS(=O)(=O)CCCS OBDVFOBWBHMJDG-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 125000003545 alkoxy group Chemical group 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000005229 chemical vapour deposition Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000003989 dielectric material Substances 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 125000005842 heteroatom Chemical group 0.000 description 2
- 238000001465 metallisation Methods 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- 238000000059 patterning Methods 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 239000002210 silicon-based material Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 159000000000 sodium salts Chemical class 0.000 description 2
- 125000001544 thienyl group Chemical group 0.000 description 2
- UMGDCJDMYOKAJW-UHFFFAOYSA-N thiourea Chemical compound NC(N)=S UMGDCJDMYOKAJW-UHFFFAOYSA-N 0.000 description 2
- 125000004209 (C1-C8) alkyl group Chemical group 0.000 description 1
- WGJCBBASTRWVJL-UHFFFAOYSA-N 1,3-thiazolidine-2-thione Chemical compound SC1=NCCS1 WGJCBBASTRWVJL-UHFFFAOYSA-N 0.000 description 1
- FHTDDANQIMVWKZ-UHFFFAOYSA-N 1h-pyridine-4-thione Chemical compound SC1=CC=NC=C1 FHTDDANQIMVWKZ-UHFFFAOYSA-N 0.000 description 1
- RILZRCJGXSFXNE-UHFFFAOYSA-N 2-[4-(trifluoromethoxy)phenyl]ethanol Chemical compound OCCC1=CC=C(OC(F)(F)F)C=C1 RILZRCJGXSFXNE-UHFFFAOYSA-N 0.000 description 1
- FULCXPQDMXUVSB-UHFFFAOYSA-N 3-(3-sulfanylpropylsulfonyloxy)propane-1-sulfonic acid Chemical compound OS(=O)(=O)CCCOS(=O)(=O)CCCS FULCXPQDMXUVSB-UHFFFAOYSA-N 0.000 description 1
- REEBJQTUIJTGAL-UHFFFAOYSA-N 3-pyridin-1-ium-1-ylpropane-1-sulfonate Chemical compound [O-]S(=O)(=O)CCC[N+]1=CC=CC=C1 REEBJQTUIJTGAL-UHFFFAOYSA-N 0.000 description 1
- 239000005749 Copper compound Substances 0.000 description 1
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 1
- BWGNESOTFCXPMA-UHFFFAOYSA-N Dihydrogen disulfide Chemical compound SS BWGNESOTFCXPMA-UHFFFAOYSA-N 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical group C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- PDQAZBWRQCGBEV-UHFFFAOYSA-N Ethylenethiourea Chemical compound S=C1NCCN1 PDQAZBWRQCGBEV-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 1
- 229920002594 Polyethylene Glycol 8000 Polymers 0.000 description 1
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 1
- NSOXQYCFHDMMGV-UHFFFAOYSA-N Tetrakis(2-hydroxypropyl)ethylenediamine Chemical compound CC(O)CN(CC(C)O)CCN(CC(C)O)CC(C)O NSOXQYCFHDMMGV-UHFFFAOYSA-N 0.000 description 1
- 229920002359 Tetronic® Polymers 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Natural products NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 125000003710 aryl alkyl group Chemical group 0.000 description 1
- 125000004429 atom Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 125000000499 benzofuranyl group Chemical group O1C(=CC2=C1C=CC=C2)* 0.000 description 1
- IOJUPLGTWVMSFF-UHFFFAOYSA-N benzothiazole Chemical compound C1=CC=C2SC=NC2=C1 IOJUPLGTWVMSFF-UHFFFAOYSA-N 0.000 description 1
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 150000004657 carbamic acid derivatives Chemical class 0.000 description 1
- 125000002837 carbocyclic group Chemical group 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 229960004106 citric acid Drugs 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 230000000536 complexating effect Effects 0.000 description 1
- 239000008139 complexing agent Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 150000001880 copper compounds Chemical class 0.000 description 1
- 229910000365 copper sulfate Inorganic materials 0.000 description 1
- JZCCFEFSEZPSOG-UHFFFAOYSA-L copper(II) sulfate pentahydrate Chemical compound O.O.O.O.O.[Cu+2].[O-]S([O-])(=O)=O JZCCFEFSEZPSOG-UHFFFAOYSA-L 0.000 description 1
- OPQARKPSCNTWTJ-UHFFFAOYSA-L copper(ii) acetate Chemical class [Cu+2].CC([O-])=O.CC([O-])=O OPQARKPSCNTWTJ-UHFFFAOYSA-L 0.000 description 1
- 125000000332 coumarinyl group Chemical group O1C(=O)C(=CC2=CC=CC=C12)* 0.000 description 1
- VJFMSYZSFUWQPZ-MBZVMHRFSA-N cupreine Chemical compound C1=C(O)C=C2C([C@H]([C@@H]3[N@]4CC[C@H]([C@H](C4)C=C)C3)O)=CC=NC2=C1 VJFMSYZSFUWQPZ-MBZVMHRFSA-N 0.000 description 1
- 125000004093 cyano group Chemical group *C#N 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 125000000753 cycloalkyl group Chemical group 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- VJFMSYZSFUWQPZ-UHFFFAOYSA-N demethyl quinine Natural products C1=C(O)C=C2C(C(C3N4CCC(C(C4)C=C)C3)O)=CC=NC2=C1 VJFMSYZSFUWQPZ-UHFFFAOYSA-N 0.000 description 1
- 150000004985 diamines Chemical class 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 229960001484 edetic acid Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007772 electroless plating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 125000002541 furyl group Chemical group 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 125000002883 imidazolyl group Chemical group 0.000 description 1
- 125000001041 indolyl group Chemical group 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 125000004573 morpholin-4-yl group Chemical group N1(CCOCC1)* 0.000 description 1
- LNOPIUAQISRISI-UHFFFAOYSA-N n'-hydroxy-2-propan-2-ylsulfonylethanimidamide Chemical compound CC(C)S(=O)(=O)CC(N)=NO LNOPIUAQISRISI-UHFFFAOYSA-N 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 description 1
- 239000006259 organic additive Substances 0.000 description 1
- 125000002971 oxazolyl group Chemical group 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229920002120 photoresistant polymer Polymers 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000007517 polishing process Methods 0.000 description 1
- 229920001983 poloxamer Polymers 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 1
- LJCNRYVRMXRIQR-OLXYHTOASA-L potassium sodium L-tartrate Chemical compound [Na+].[K+].[O-]C(=O)[C@H](O)[C@@H](O)C([O-])=O LJCNRYVRMXRIQR-OLXYHTOASA-L 0.000 description 1
- 229940074439 potassium sodium tartrate Drugs 0.000 description 1
- 230000002028 premature Effects 0.000 description 1
- KCXFHTAICRTXLI-UHFFFAOYSA-N propane-1-sulfonic acid Chemical compound CCCS(O)(=O)=O KCXFHTAICRTXLI-UHFFFAOYSA-N 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 125000003373 pyrazinyl group Chemical group 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 125000004076 pyridyl group Chemical group 0.000 description 1
- 125000000714 pyrimidinyl group Chemical group 0.000 description 1
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 description 1
- 125000000168 pyrrolyl group Chemical group 0.000 description 1
- 238000004626 scanning electron microscopy Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 235000011006 sodium potassium tartrate Nutrition 0.000 description 1
- 238000004528 spin coating Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000003871 sulfonates Chemical class 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011975 tartaric acid Substances 0.000 description 1
- 235000002906 tartaric acid Nutrition 0.000 description 1
- 229960001367 tartaric acid Drugs 0.000 description 1
- 125000003718 tetrahydrofuranyl group Chemical group 0.000 description 1
- 125000001412 tetrahydropyranyl group Chemical group 0.000 description 1
- 125000000335 thiazolyl group Chemical group 0.000 description 1
- 150000003852 triazoles Chemical class 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000000080 wetting agent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/48—After-treatment of electroplated surfaces
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/38—Electroplating: Baths therefor from solutions of copper
-
- 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
- H05K3/40—Forming printed elements for providing electric connections to or between printed circuits
- H05K3/42—Plated through-holes or plated via connections
- H05K3/423—Plated through-holes or plated via connections characterised by electroplating method
Definitions
- the present invention relates to copper electroplating solutions, methods for using the solutions and products formed by using such methods and solutions. More particularly, the invention provides electrolytic copper plating solutions that have increased brightener levels and use of same for effective plating of high aspect ratio apertures, e.g. microvias with aspect ratios of at least 4:1 and diameters of 200 nm or smaller.
- high aspect ratio apertures e.g. microvias with aspect ratios of at least 4:1 and diameters of 200 nm or smaller.
- Electroplating articles with copper coatings is generally well known in the industry. Electroplating methods involve passing a current between two electrodes in a plating solution where one electrode is the article to be plated.
- a common plating solution would be an acid copper plating solution containing (1) a dissolved copper salt (such as copper sulfate), (2) an acidic electrolyte (such as sulfuric acid) in an amount sufficient to impart conductivity to the bath and (3) additives (such as surfactants, brighteners, levelers and suppressants) to enhance the effectiveness and quality of plating. See generally U.S. Pat. Nos. 5,668,013; 5,174,886; 5,051,154; 3,876,513; and 5,068,013 for a discussion of copper plating baths.
- Copper plating technology has been particularly important in the manufacture of computer circuit boards. More specifically, during circuit board manufacture, copper electrical connections are provided between various board layers by plating board through holes whereby a thin conductive copper conductive is first applied, typically using electroless copper plating techniques, followed by electroplating copper from acid copper Solutions.
- Copper plating is also employed in circuit board manufacture to plate outer layers where final circuitry is defined.
- panel plating is typically employed, where the full circuit board surface is copper plated followed by photodefining circuitry with a photoresist and then etching in a subtractive process.
- an additive process can be employed, where copper circuits are produced by plating between lines defined by a resist relief image.
- reactive ion etching is not practical as a result of the paucity of copper compounds with vapor pressures sufficient to enable removal of the copper as may be desired.
- Damascene process starts with deposition of dielectric typically by chemical vapor deposition of silicon materials or organic dielectrics followed by curing, or spin coating silicon materials or organic dielectrics. Patterning by photolithographic processes and reactive ion etching defines the vias and trenches (interconnects) in the dielectric.
- Barrier layers are then formed by chemical vapor deposition or other methods to isolate the copper lines from the dielectric. Copper is then deposited and excess material removed by chemical or mechanical polishing processes.
- defects such as seams, voids and inclusions can occur with conventional methods when attempting to plate features that are smaller or have higher aspect ratios.
- defects can occur as a result of conformal copper plating, i.e. where all targeted surfaces are plated at the same rate such that the sidewalls of a via or trench plate together forming a seam or a demarcation of disruption where the copper grains are separated and will not anneal to form a continuous copper wire.
- Defects also will occur at the top rim of a via hole, where electronic charge density can concentrate and result in rapid copper growth that closes off the via before the via is filled sufficiently with metal.
- Such inadequate metal fill can result in inclusion and voids, disrupting the ability of the plated metal to carry a coherent signal.
- compositions and methods of the invention are particularly useful for filling microvias and trenches required by current and anticipated semiconductor fabrication requirements (including microvias having aspect ratios of at least 4:1 and diameters of 200 nm or less) by reliably plating copper deposits that are essentially or completely free of voids, inclusions or other plating imperfections.
- Electroplating baths of the invention are characterized in significant part by comprising enhanced brightener concentrations. Without being bound by any theory, it is believed that the higher brightener concentrations can accelerate the plating rate in recesses and microvias as carrier molecules become incorporated into the plating deposit. This is counterintuitive to conventional thought and a completely unexpected result.
- preferred electroplating compositions of the invention have a brightener concentration of at least about 1.5 mg per liter of plating solution (1.5 mg/L), more preferably a brightener concentration of at least about 1.75 mg per liter, still more preferably at least about 2.0, 2.5. 3, 3.5 or 4 mg of brightener per liter of plating solution.
- Good results have been achieved with even higher brightener concentrations, e.g. copper plating baths having a brightener concentration of at least about 5 mg per liter, or at least about 6, 7, 8, 9, 10, 12, 14, 16, 18, 20 or 25 mg/L, or even higher brightener concentrations such as at least about 30, 35, 40, 45, 50, 55 or 60 mg of brightener per liter of plating solution.
- the brightener concentration is maintained at such high concentrations throughout the entire or at least substantial portion of a plating cycle.
- Such maintenance of brightener concentrations entails regular addition of brightener during a plating cycle as the brightener component plates out.
- Brightener concentrations and replenishment rates during a plating cycle can be readily determined by known methods, such as the CPVS method as disclosed in U.S. Pat. Nos. 5,252,196 and 5,223,118, both assigned to the Shipley Company, or by the cyclic voltammetric stripping (CVS) methods.
- CVS cyclic voltammetric stripping
- the plating bath also contains a surfactant-type suppressor agent.
- a surfactant-type suppressor agent in addition to such an elevated brightener concentration, preferably the plating bath also contains a surfactant-type suppressor agent. It has been surprisingly found that use of such a suppressor agent in combination with elevated brightener concentrations can result in effective “bottom-fill” copper plating of a microvia or other aperture without defects such as inclusions or voids.
- the suppressor enables enhanced plating rate at the bottom of a microvia, permitting copper to plate the entire aperture space in a substantially “bottom-fill” manner, without premature sealing of the aperture top that can result in inclusions or voids.
- the invention also includes articles of manufacture, including electronic packaging devices such as printed circuit boards, multichip modules, semiconductor integrated circuits and the like that contain a copper deposit produced from a plating solution of the invention. Other aspects of the invention are discussed infra
- Compositions of the invention suitably contain a copper salt, an electrolyte preferably an acidic aqueous solution such as a sulfuric acid solution with a chloride or other halide ion source, and one or more brightener agents in enhanced concentrations as discussed above, and preferably a suppressor agent.
- the plating compositions also may contain other components such as one or more leveler agents and the like.
- electroplating solutions of the invention are particularly effective in plating various articles having microvias with high aspect ratios and small diameters.
- solutions of the invention are useful in plating electronic packaging devices such as printed circuit boards, microchip module packaging and blind 3-dimensional structures, particularly semiconductor integrated circuits and other circuit systems.
- the electroplating solutions of the invention are particularly useful to copper fill microvias of such electronic devices without the defects exhibited upon use of prior chemistries.
- the invention has application to plating on a wide variety of other polymer and metal substrates.
- Electroplating solutions of the invention generally comprise at least one soluble copper salt, an electrolyte and a brightener component. More particularly, electroplating compositions of the invention preferably contain a copper salt; an electrolyte, preferably an acidic aqueous solution such as a sulfuric acid solution with a chloride or other halide ion source; and one or more brightener agents in enhanced concentrations as discussed above. Electroplating compositions of the invention also preferably contain a suppressor agent. The plating compositions also may contain other components such as one or more leveler agents and the like.
- a variety of copper salts may be employed in the subject electroplating solutions, including for example copper sulfates, copper acetates, copper fluoroborate, and cupric nitrates. Copper sulfate pentahydrate is a particularly preferred copper salt.
- a copper salt may be suitably present in a relatively wide concentration range in the electroplating compositions of the invention. Preferably, a copper salt will be employed at a concentration of from about 10 to about 300 grams per liter of plating solution, more preferably at a concentration of from about 25 to about 200 grams per liter of plating solution, still more preferably at a concentration of from about 40 to about 175 grams per liter of plating solution.
- Plating baths of the invention preferably employ an acidic electrolyte, which typically will be an acidic aqueous solution and that preferably contains a halide ion source, particularly a chloride ion source.
- suitable acids for the electrolyte include sulfuric acid, acetic acid, fluoroboric acid, methane sulfonic acid and sulfamic acid. Sulfuric acid is generally preferred.
- Chloride is a generally preferred halide ion.
- a wide range of halide ion concentrations (if a halide ion is employed) may be suitably utilized, e.g. from about 0 (where no halide ion employed) to 100 parts per million (ppm) of halide ion in the plating solution, more preferably from about 25 to about 75 ppm of halide ion source in the plating solution.
- the invention also includes electroplating baths that are substantially or completely free of an added acid and may be neutral or essentially neutral (e.g. pH of at least less than about 8 or 8.5).
- Such plating compositions are suitably prepared in the same manner with the same components as other compositions disclosed herein but without an added acid.
- a preferred substantially neutral plating composition of the invention may have the same components as the plating bath of Example I which follows, but without the addition of sulfuric acid.
- copper electroplating compositions are provided that have a brightener agent concentration of at least about 1.5 mg per liter of plating solution (1.5 mg/L), compared to typical brightener concentrations ranging from about 0.05 to 1.0 mg/L in prior composition. More preferably, in electroplating baths of the invention, the brightener concentration is at least about 1.75 mg/L, and still more preferably, at least about 2, 2.5, 3, 3.5 or 4 mg/L. Even higher brightener concentrations will be suitable or even preferred, e.g. at least about 10, 15, 20, 30, 40, 50 mg of brightener per liter of plating solution. A brightener concentration of from about 20 to about 200 mg per liter of plating solution will be suitable for many applications.
- the brightener concentration is maintained throughout the entire electroplating process, or throughout at least a substantial portion of the plating process, e.g. at least about 50, 60, 70, 80 or 90 percent of the duration of the plating process.
- the brightener component is preferably regularly replenished during plating to maintain a steady state brightener concentration.
- a wide variety of brighteners may be employed in the copper electroplating compositions of the invention.
- Typical brighteners contain one or more sulfur atoms, and typically without any nitrogen atoms and a molecular weight of about 1000 or less.
- Brightener compounds that have sulfide and/or sulfonic acid groups are generally preferred, particularly compounds that comprise a group of the formula R′—S—R—SO 3 X, where R is an optionally substituted alkyl (which include cycloalkyl), optionally substituted heteroalkyl, optionally substituted aryl group, or optionally substituted heteroalicyclic; X is a counter ion such as sodium or potassium; and R′ is hydrogen or a chemical bond (i.e. —S—R—SO 3 X or substituent of a larger compound).
- alkyl groups will have from one to about 16 carbons, more typically one to about 8 or 12 carbons.
- Heteroalkyl groups will have one or more hetero (N, O or S) atoms in the chain, and preferably have from 1 to about 16 carbons, more typically 1 to about 8 or 12 carbons.
- Carbocyclic aryl groups are typical aryl groups, such as phenyl and naphthyl.
- Heteroaromatic groups also will be suitable aryl groups, and typically contain 1 to about 3 N, O or S atoms and 1-3 separate or fused rings and include e.g.
- Heteroalicyclic groups typically will have 1 to 3 N, O or S atoms and from 1 to 3 separate or fused rings and include e.g. tetrahydrofuranyl, thienyl, tetrahydropyranyl, piperdinyl, morpholino, pyrrolindinyl, and the like.
- Substituents of substituted alkyl, heteroalkyl, aryl or heteroalicyclic groups include e.g. C 1-8 alkoxy; C 1-8 alkyl, halogen, particularly F, Cl and Br; cyano, nitro, and the like.
- useful brighteners include those of the following formulae:
- R is an optionally substituted alkyl group, and preferably is an alkyl group having from 1 to 6 carbon atoms, more preferably is an alkyl group having from 1 to 4 carbon atoms;
- Ar is an optionally substituted aryl group such as optionally substituted phenyl or naphthyl; and
- X is a suitable counter ion such as sodium or potassium.
- Some specific suitable brighteners include e.g. n,n-dimethyl-dithiocarbamic acid-(3-sulfopropyl)ester; 3-mercapto-propylsulfonic acid-(3-sulfopropyl)ester; 3-mercapto-propylsulfonic acid (sodium salt); carbonic acid-dithio-o-ethylester-s-ester with 3-mercapto-l-propane sulfonic acid (potassium salt); bissulfopropyl disulfide; 3-(benzthiazolyl-s-thio)propyl sulfonic acid (sodium salt); pyridinium propyl sulfobetaine; 1-sodium-3-mercaptopropane-l-sulfonate; sulfoalkyl sulfide compounds disclosed in U.S.
- plating baths of the invention optionally may contain a variety of other components, including organic additives such as suppressors agents, leveling agents and the like.
- a suppressor agent in combination with an enhanced brightener concentration is particularly preferred and provides surprisingly enhanced plating performance, particularly in bottom-fill plating of small diameter and/or high aspect ratio microvias.
- the suppressor agent concentration remains relatively constant and at an elevated level relative to the microvia bottom regions. Consequently, the area at a microvia top has a comparatively suppressed plating rate because of the enhanced suppressor agent concentration relative to the microvia bottom regions.
- Preferred suppressor agents for use in the compositions of the invention are polymeric materials, preferably s having hetero atom substitution, particularly oxygen linkages.
- Generally preferred suppressor agents ate generally high molecular weight polyethers, such as those of the following formula:
- R is an aryl or alkyl group containing from about 2 to 20 carbon atoms; each X, Y, X′ and Y′ is independently hydrogen; alkyl preferably methyl, ethyl or propyl; aryl such as phenyl; aralkyl such as benzyl, and preferably one or more of X, Y, X′ and Y′ is hydrogen; and n is an integer between 5 and 100,000.
- R is ethylene and n is greater than 12,000.
- surfactants useful in the present invention include e.g. amines such as ethoxylated amines, polyoxyalkylene amines and alkanol amines; amides; polyglycol-type wetting agents, such as polyethylene glycols, polyalkylene glycols and polyoxyalkyene glycols; high molecular weight polyethers; polyethylene oxides (mol. wt.
- Particularly suitable surfactants for plating compositions of the invention are commercially available polyethylene glycol copolymers, including polyethylene glycol copolymers.
- polyethylene glycol copolymers are available from e.g. BASF (sold by BASF under Tetronic and Pluronic tradenames), and copolymers from Chemax.
- BASF sold by BASF under Tetronic and Pluronic tradenames
- Chemax copolymers from Chemax.
- a butylalcoholethylene oxide-propylene oxide copolymer having an M w of about 1800 from Chemax is particularly preferred.
- Surfactants are typically added to copper electroplating solutions in concentrations ranging from about 1 to 10,000 ppm based on the weight of the bath, more preferably about 5 to 10,000 ppm.
- leveling agents Use of one or more leveling agents in plating baths of the invention is generally preferred. Examples of suitable leveling agents are described and set forth in U.S. Pat. Nos. 3,770,598, 4,374,709, 4,376,685, 4,555,315 and 4,673,459.
- useful leveling agents include those that contain a substituted amino group such as compounds having R—N—R′, where each R and R′ is independently a substituted or unsubstituted alkyl group or a substituted or unsubstituted aryl group.
- the alkyl groups have from 1 to 6 carbon atoms, more typically from 1 to 4 carbon atoms.
- Suitable aryl groups include substituted or unsubstituted phenyl or naphthyl.
- the substituents of the substituted alkyl and aryl groups may be, for example, alkyl, halo and alkoxy.
- suitable leveling agents include e.g. 1-(2-hydroxyethyl)-2-imidazolidinethione; 4-mercaptopyridine; 2-mercaptothiazoline; ethylene thiourea; thiourea; alkylated polyalkyleneimine; phenazonium compounds disclosed in U.S. Pat. No. 3,956,084; N-heteroaromatic rings containing polymers; quaternized, acrylic, polymeric amines; polyvinyl carbamates; pyrrolidone; and imidazole.
- a particularly preferred leveler is 1-(2-hydroxyethyl)-2-imidazolidinethione. Typical concentrations of leveling agents range from about 0.05 to 0.5 mg per liter of plating solution.
- the copper electroplating compositions are suitably used in similar manner as prior copper electroplating baths, except an elevated brightener concentration is employed and preferably maintained at an elevated level throughout a plating cycle.
- a copper clad plastic substrate is typically employed, e.g. a copper clad glass fiber reinforced epoxy panel.
- apertures Prior to formation of a circuit, apertures, such as microvias, are formed in the board by drilling and metallization. Microvias and other apertures also may be formed by photoimaging. Processes for forming such apertures in electronic device substrates are known and are disclosed e.g. in U.S. Pat. No. 4,902,610; C. Coombs, Printed Circuits Handbook , (4 th ed., McGraw Hill); and T. Kiko, Printed Circuit Board Basics (PMS Indus.).
- electroless plating procedures are then used to form a first metallic coating over the substrate surfaces and electrolytic copper deposition is then used to enhance the thickness of the coating.
- electrolytic copper may be plated directly over a suitably prepared microvia as disclosed in any of U.S. Pat. Nos. 5,425,873; 5,207,888; and 4,919,768.
- the next step in the process comprises electroplating copper onto the thus prepared conductive microvias using an electroplating solution of the invention.
- Plating baths of the invention are preferably employed at or above room temperature, e.g. up to and somewhat above 65° C.
- the plating composition is preferably agitated during use such as by air sparger, work piece agitation, impingement or other suitable method.
- Plating is preferably conducted at a current ranging from 1 to 40 ASF depending upon substrate characteristics.
- Plating time may range from about 5 minutes to 1 hour or more, depending on the difficulty of the work piece. See generally the examples which follow for exemplary preferred procedures.
- compositions of the invention are particularly useful to plate difficult work pieces, such as circuit board substrates with small diameter, high aspect ratio microvias and other apertures.
- the plating compositions of the invention also will be particularly useful for plating integrated circuit devices, such as formed semiconductor devices and the like. See the examples which follow for exemplary substrates plated in accordance with the invention.
- aspect ratios of at least 4:1, having diameters of about 200 nm or smaller have been effectively copper plated with no defects (e.g. no voids or inclusions by ion beam examination) using plating solutions of the invention.
- Microvias with diameters below 150 nm, or even below about 100 nm, and aspect ratios of 5:1, 6:1, 7:1, 10:1 or greater, and even up to about 15:1 or greater can be effectively plated (e.g. no voids or inclusions by ion beam examination) using plating solutions of the invention.
- a preferred copper electroplating bath of the invention was prepared by admixing the following components in water.
- the brightener was bis-sodium-sulfonopropyl-disulfide and the suppressor was a polyethylene glycol polymer sold under the tradename PEG 8000 by Union Carbide.
- Component Concentration CuSO 4 5H 2 O 60 g/l H 2 SO 4 225 g/l Cl 50 ppm Suppressor 1 g/l Brightener 2.1 mg/l
- a further preferred copper electroplating bath of the invention was prepared by admixing the following components in water.
- the brightener was bis-sodium-sulfonopropyl-disulfide and the suppressor was a propylene glycol copolymer sold under the tradename L62D by BASF.
- Component Concentration CuSO 4 5H 2 O 70 g/l H 2 SO 4 175 g/l Cl 50 ppm Suppressor 0.875 g/l Brightener 2.4 mg/l
- a further preferred copper electroplating bath of the invention was prepared by admixing the following components in water.
- the brightener was bis-sodium-sulfonopropyl-disulfide and the suppressor was a propylene glycol copolymer sold under the tradename L62D by BASF.
- Component Concentration CuSO 4 5H 2 O 60 g/l H 2 SO 4 225 g/l Cl 50 ppm Suppressor 1 g/l Brightener 0.35 mg/l
- microvias of a semiconductor microchip wafer were plated using the above comparative plating composition under conditions as described in Example 2. After termination of the plating procedure, the microvias were examined by scanning electron microscopy (SEM) and focused ion beam examination. Those examinations showed the copper deposits in the microvias contained defects of voids, seams and inclusions.
- SEM scanning electron microscopy
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Abstract
The present invention provides inter alia copper electroplating compositions, methods for use of the compositions and products formed by the compositions. Electroplating compositions of the invention contain an increased brightener concentration that can provide effective copper plate on difficult-to-plate aperture walls, including high aspect ratio, small diameter microvias.
Description
- 1. Field of the Invention
- The present invention relates to copper electroplating solutions, methods for using the solutions and products formed by using such methods and solutions. More particularly, the invention provides electrolytic copper plating solutions that have increased brightener levels and use of same for effective plating of high aspect ratio apertures, e.g. microvias with aspect ratios of at least 4:1 and diameters of 200 nm or smaller.
- 2. Background
- Electroplating articles with copper coatings is generally well known in the industry. Electroplating methods involve passing a current between two electrodes in a plating solution where one electrode is the article to be plated. A common plating solution would be an acid copper plating solution containing (1) a dissolved copper salt (such as copper sulfate), (2) an acidic electrolyte (such as sulfuric acid) in an amount sufficient to impart conductivity to the bath and (3) additives (such as surfactants, brighteners, levelers and suppressants) to enhance the effectiveness and quality of plating. See generally U.S. Pat. Nos. 5,668,013; 5,174,886; 5,051,154; 3,876,513; and 5,068,013 for a discussion of copper plating baths.
- Over time, a number of improvements in electroplating techniques have been made as the articles to be plated evolved in degree of difficulty and standards for plating increased. However, even with the improvements in electroplating techniques, circumstances exist that can lead to plating defects.
- Copper plating technology has been particularly important in the manufacture of computer circuit boards. More specifically, during circuit board manufacture, copper electrical connections are provided between various board layers by plating board through holes whereby a thin conductive copper conductive is first applied, typically using electroless copper plating techniques, followed by electroplating copper from acid copper Solutions.
- Copper plating is also employed in circuit board manufacture to plate outer layers where final circuitry is defined. For such applications, panel plating is typically employed, where the full circuit board surface is copper plated followed by photodefining circuitry with a photoresist and then etching in a subtractive process. Alternatively an additive process can be employed, where copper circuits are produced by plating between lines defined by a resist relief image.
- More recently, copper plating also has been employed in semiconductor chip manufacture to provide chip interconnections. Traditionally, semiconductors have been interconnected through aluminum conductors. However, industry continually demands enhanced performance, including ultra large-scale integration and faster circuits. Consequently, chip interconnects are required at dimensions of 200 nm and less. At such geometries, the resistivity of aluminum (theoretically 2.65×10−8 ohm/meter at room temperature) is considered too high to allow the electronic signal to pass at required speeds. Copper, with a theoretical resistivity of 1.678×10−8 ohm/meter, is considered a more suitable material to meet the next generation of semiconductor microchips.
- Typical processes for defining semiconductor chip interconnects, particularly aluminum interconnects, have involved reactive ion etching of metal layers, e.g. a process that includes metal deposition, photolithographic patterning, line definition through reactive ion etching and dielectric deposition. However, in Cu-based systems, reactive ion etching is not practical as a result of the paucity of copper compounds with vapor pressures sufficient to enable removal of the copper as may be desired.
- Consequently, alternative strategies have developed, such as the Damascene process. That process starts with deposition of dielectric typically by chemical vapor deposition of silicon materials or organic dielectrics followed by curing, or spin coating silicon materials or organic dielectrics. Patterning by photolithographic processes and reactive ion etching defines the vias and trenches (interconnects) in the dielectric.
- Barrier layers are then formed by chemical vapor deposition or other methods to isolate the copper lines from the dielectric. Copper is then deposited and excess material removed by chemical or mechanical polishing processes.
- Although conventional copper plating systems can be suitable for plating vias and trenches as small as 300 nm with 4:1 aspect ratios, defects such as seams, voids and inclusions can occur with conventional methods when attempting to plate features that are smaller or have higher aspect ratios. Such defects can occur as a result of conformal copper plating, i.e. where all targeted surfaces are plated at the same rate such that the sidewalls of a via or trench plate together forming a seam or a demarcation of disruption where the copper grains are separated and will not anneal to form a continuous copper wire. Defects also will occur at the top rim of a via hole, where electronic charge density can concentrate and result in rapid copper growth that closes off the via before the via is filled sufficiently with metal. Such inadequate metal fill can result in inclusion and voids, disrupting the ability of the plated metal to carry a coherent signal.
- It thus would be desirable to have new electroplating compositions. It would be particularly desirable to have new copper electroplating compositions that can plate effectively (e.g. absence of voids, inclusions and seams) high aspect ratio apertures, including high aspect ratio microvias as discussed above.
- We have now found copper electroplating compositions that effectively plate a wide variety of articles, including printed circuit boards and other electronic packaging devices. Compositions and methods of the invention are particularly useful for filling microvias and trenches required by current and anticipated semiconductor fabrication requirements (including microvias having aspect ratios of at least 4:1 and diameters of 200 nm or less) by reliably plating copper deposits that are essentially or completely free of voids, inclusions or other plating imperfections.
- Electroplating baths of the invention are characterized in significant part by comprising enhanced brightener concentrations. Without being bound by any theory, it is believed that the higher brightener concentrations can accelerate the plating rate in recesses and microvias as carrier molecules become incorporated into the plating deposit. This is counterintuitive to conventional thought and a completely unexpected result.
- In particular, preferred electroplating compositions of the invention have a brightener concentration of at least about 1.5 mg per liter of plating solution (1.5 mg/L), more preferably a brightener concentration of at least about 1.75 mg per liter, still more preferably at least about 2.0, 2.5. 3, 3.5 or 4 mg of brightener per liter of plating solution. Good results have been achieved with even higher brightener concentrations, e.g. copper plating baths having a brightener concentration of at least about 5 mg per liter, or at least about 6, 7, 8, 9, 10, 12, 14, 16, 18, 20 or 25 mg/L, or even higher brightener concentrations such as at least about 30, 35, 40, 45, 50, 55 or 60 mg of brightener per liter of plating solution.
- Preferably, the brightener concentration is maintained at such high concentrations throughout the entire or at least substantial portion of a plating cycle. Such maintenance of brightener concentrations entails regular addition of brightener during a plating cycle as the brightener component plates out. Brightener concentrations and replenishment rates during a plating cycle can be readily determined by known methods, such as the CPVS method as disclosed in U.S. Pat. Nos. 5,252,196 and 5,223,118, both assigned to the Shipley Company, or by the cyclic voltammetric stripping (CVS) methods.
- In addition to such an elevated brightener concentration, preferably the plating bath also contains a surfactant-type suppressor agent. It has been surprisingly found that use of such a suppressor agent in combination with elevated brightener concentrations can result in effective “bottom-fill” copper plating of a microvia or other aperture without defects such as inclusions or voids. In particular, the suppressor enables enhanced plating rate at the bottom of a microvia, permitting copper to plate the entire aperture space in a substantially “bottom-fill” manner, without premature sealing of the aperture top that can result in inclusions or voids.
- The invention also includes articles of manufacture, including electronic packaging devices such as printed circuit boards, multichip modules, semiconductor integrated circuits and the like that contain a copper deposit produced from a plating solution of the invention. Other aspects of the invention are discussed infra
- Compositions of the invention suitably contain a copper salt, an electrolyte preferably an acidic aqueous solution such as a sulfuric acid solution with a chloride or other halide ion source, and one or more brightener agents in enhanced concentrations as discussed above, and preferably a suppressor agent. The plating compositions also may contain other components such as one or more leveler agents and the like.
- As discussed above, electroplating solutions of the invention are particularly effective in plating various articles having microvias with high aspect ratios and small diameters. In particular, solutions of the invention are useful in plating electronic packaging devices such as printed circuit boards, microchip module packaging and blind 3-dimensional structures, particularly semiconductor integrated circuits and other circuit systems. The electroplating solutions of the invention are particularly useful to copper fill microvias of such electronic devices without the defects exhibited upon use of prior chemistries. In addition, the invention has application to plating on a wide variety of other polymer and metal substrates.
- Electroplating solutions of the invention generally comprise at least one soluble copper salt, an electrolyte and a brightener component. More particularly, electroplating compositions of the invention preferably contain a copper salt; an electrolyte, preferably an acidic aqueous solution such as a sulfuric acid solution with a chloride or other halide ion source; and one or more brightener agents in enhanced concentrations as discussed above. Electroplating compositions of the invention also preferably contain a suppressor agent. The plating compositions also may contain other components such as one or more leveler agents and the like.
- A variety of copper salts may be employed in the subject electroplating solutions, including for example copper sulfates, copper acetates, copper fluoroborate, and cupric nitrates. Copper sulfate pentahydrate is a particularly preferred copper salt. A copper salt may be suitably present in a relatively wide concentration range in the electroplating compositions of the invention. Preferably, a copper salt will be employed at a concentration of from about 10 to about 300 grams per liter of plating solution, more preferably at a concentration of from about 25 to about 200 grams per liter of plating solution, still more preferably at a concentration of from about 40 to about 175 grams per liter of plating solution.
- Plating baths of the invention preferably employ an acidic electrolyte, which typically will be an acidic aqueous solution and that preferably contains a halide ion source, particularly a chloride ion source. Examples of suitable acids for the electrolyte include sulfuric acid, acetic acid, fluoroboric acid, methane sulfonic acid and sulfamic acid. Sulfuric acid is generally preferred. Chloride is a generally preferred halide ion. A wide range of halide ion concentrations (if a halide ion is employed) may be suitably utilized, e.g. from about 0 (where no halide ion employed) to 100 parts per million (ppm) of halide ion in the plating solution, more preferably from about 25 to about 75 ppm of halide ion source in the plating solution.
- The invention also includes electroplating baths that are substantially or completely free of an added acid and may be neutral or essentially neutral (e.g. pH of at least less than about 8 or 8.5). Such plating compositions are suitably prepared in the same manner with the same components as other compositions disclosed herein but without an added acid. Thus, for instance, a preferred substantially neutral plating composition of the invention may have the same components as the plating bath of Example I which follows, but without the addition of sulfuric acid.
- As discussed above, it has been discovered that by increasing brightener concentration beyond conventional levels, uniform plating of particularly high aspect ratio microvias and other difficult-to-plate apertures is now possible.
- In particular, copper electroplating compositions are provided that have a brightener agent concentration of at least about 1.5 mg per liter of plating solution (1.5 mg/L), compared to typical brightener concentrations ranging from about 0.05 to 1.0 mg/L in prior composition. More preferably, in electroplating baths of the invention, the brightener concentration is at least about 1.75 mg/L, and still more preferably, at least about 2, 2.5, 3, 3.5 or 4 mg/L. Even higher brightener concentrations will be suitable or even preferred, e.g. at least about 10, 15, 20, 30, 40, 50 mg of brightener per liter of plating solution. A brightener concentration of from about 20 to about 200 mg per liter of plating solution will be suitable for many applications.
- Preferably, the brightener concentration is maintained throughout the entire electroplating process, or throughout at least a substantial portion of the plating process, e.g. at least about 50, 60, 70, 80 or 90 percent of the duration of the plating process. As discussed above, since brightener levels are depleted as the electroplating progresses, the brightener component is preferably regularly replenished during plating to maintain a steady state brightener concentration.
- A wide variety of brighteners, including known brightener agents, may be employed in the copper electroplating compositions of the invention. Typical brighteners contain one or more sulfur atoms, and typically without any nitrogen atoms and a molecular weight of about 1000 or less. Brightener compounds that have sulfide and/or sulfonic acid groups are generally preferred, particularly compounds that comprise a group of the formula R′—S—R—SO3X, where R is an optionally substituted alkyl (which include cycloalkyl), optionally substituted heteroalkyl, optionally substituted aryl group, or optionally substituted heteroalicyclic; X is a counter ion such as sodium or potassium; and R′ is hydrogen or a chemical bond (i.e. —S—R—SO3X or substituent of a larger compound). Typically alkyl groups will have from one to about 16 carbons, more typically one to about 8 or 12 carbons. Heteroalkyl groups will have one or more hetero (N, O or S) atoms in the chain, and preferably have from 1 to about 16 carbons, more typically 1 to about 8 or 12 carbons. Carbocyclic aryl groups are typical aryl groups, such as phenyl and naphthyl. Heteroaromatic groups also will be suitable aryl groups, and typically contain 1 to about 3 N, O or S atoms and 1-3 separate or fused rings and include e.g. coumarinyl, qulinolinyl, pyridyl, pyrazinyl, pyrimidyl, furyl, pyrrolyl, thienyl, thiazolyl, oxazolyl, oxidizolyl, triazole, imidazolyl, indolyl, benzofuranyl, benzothiazol, and the like. Heteroalicyclic groups typically will have 1 to 3 N, O or S atoms and from 1 to 3 separate or fused rings and include e.g. tetrahydrofuranyl, thienyl, tetrahydropyranyl, piperdinyl, morpholino, pyrrolindinyl, and the like. Substituents of substituted alkyl, heteroalkyl, aryl or heteroalicyclic groups include e.g. C1-8 alkoxy; C1-8 alkyl, halogen, particularly F, Cl and Br; cyano, nitro, and the like.
- More specifically, useful brighteners include those of the following formulae:
- XO3 S—R—SH
- XO3S—R—S—S—R—SO3 X and
- XO3S—Ar—S—S—Ar—SO3X
- where in the above formulae R is an optionally substituted alkyl group, and preferably is an alkyl group having from 1 to 6 carbon atoms, more preferably is an alkyl group having from 1 to 4 carbon atoms; Ar is an optionally substituted aryl group such as optionally substituted phenyl or naphthyl; and X is a suitable counter ion such as sodium or potassium.
- Some specific suitable brighteners include e.g. n,n-dimethyl-dithiocarbamic acid-(3-sulfopropyl)ester; 3-mercapto-propylsulfonic acid-(3-sulfopropyl)ester; 3-mercapto-propylsulfonic acid (sodium salt); carbonic acid-dithio-o-ethylester-s-ester with 3-mercapto-l-propane sulfonic acid (potassium salt); bissulfopropyl disulfide; 3-(benzthiazolyl-s-thio)propyl sulfonic acid (sodium salt); pyridinium propyl sulfobetaine; 1-sodium-3-mercaptopropane-l-sulfonate; sulfoalkyl sulfide compounds disclosed in U.S. Pat. No. 3,778,357; the peroxide oxidation product of a dialkyl amino-thiox-methyl-thioalkanesulfonic acid; and combinations of the above. Additional suitable brighteners are also described in U.S. Pat. Nos. 3,770,598, 4,374,709, 4,376,685, 4,555,315, and 4,673,469, all incorporated herein by reference. Particularly preferred brighteners for use in the plating compositions of the invention are n,n-dimethyl-dithiocarbamic acid-(3-sulfopropyl)ester and bis-sodium-sulfonopropyl-disulfide.
- In addition to the copper salts, electrolyte and brightener, plating baths of the invention optionally may contain a variety of other components, including organic additives such as suppressors agents, leveling agents and the like.
- As discussed above, use of a suppressor agent in combination with an enhanced brightener concentration is particularly preferred and provides surprisingly enhanced plating performance, particularly in bottom-fill plating of small diameter and/or high aspect ratio microvias.
- Without being bound by any theory, it is believed such enhanced bottom-fill plating may occur due to the concentration of the suppressor agent being comparatively decreased at a bottom of a microvia as a result of diffusion effects through the length of the microvia. That reduced suppressor concentration results in an enhanced copper plating rate at the microvia bottom regions.
- In contrast, at the surface of the article to be plated (at the top of the microvia), the suppressor agent concentration remains relatively constant and at an elevated level relative to the microvia bottom regions. Consequently, the area at a microvia top has a comparatively suppressed plating rate because of the enhanced suppressor agent concentration relative to the microvia bottom regions.
- Preferred suppressor agents for use in the compositions of the invention are polymeric materials, preferably s having hetero atom substitution, particularly oxygen linkages. Generally preferred suppressor agents ate generally high molecular weight polyethers, such as those of the following formula:
- R—O—(CXYCX′Y′O)nH
- where R is an aryl or alkyl group containing from about 2 to 20 carbon atoms; each X, Y, X′ and Y′ is independently hydrogen; alkyl preferably methyl, ethyl or propyl; aryl such as phenyl; aralkyl such as benzyl, and preferably one or more of X, Y, X′ and Y′ is hydrogen; and n is an integer between 5 and 100,000. Preferably, R is ethylene and n is greater than 12,000.
- More specifically, surfactants useful in the present invention include e.g. amines such as ethoxylated amines, polyoxyalkylene amines and alkanol amines; amides; polyglycol-type wetting agents, such as polyethylene glycols, polyalkylene glycols and polyoxyalkyene glycols; high molecular weight polyethers; polyethylene oxides (mol. wt. 300,000 to 4 million); block copolymers of polyoxyalkyenes; alkylpolyether sulfonates; complexing surfactants such as alkoxylated diamines; and complexing agents for cupric or cuprous ions which include entprol, citric acid, edetic acid, tartaric acid, potassium sodium tartrate, acetonitrile, cupreine and pyridine.
- Particularly suitable surfactants for plating compositions of the invention are commercially available polyethylene glycol copolymers, including polyethylene glycol copolymers. Such polymers are available from e.g. BASF (sold by BASF under Tetronic and Pluronic tradenames), and copolymers from Chemax. A butylalcoholethylene oxide-propylene oxide copolymer having an Mw of about 1800 from Chemax is particularly preferred.
- Surfactants are typically added to copper electroplating solutions in concentrations ranging from about 1 to 10,000 ppm based on the weight of the bath, more preferably about 5 to 10,000 ppm.
- Use of one or more leveling agents in plating baths of the invention is generally preferred. Examples of suitable leveling agents are described and set forth in U.S. Pat. Nos. 3,770,598, 4,374,709, 4,376,685, 4,555,315 and 4,673,459. In general, useful leveling agents include those that contain a substituted amino group such as compounds having R—N—R′, where each R and R′ is independently a substituted or unsubstituted alkyl group or a substituted or unsubstituted aryl group. Typically the alkyl groups have from 1 to 6 carbon atoms, more typically from 1 to 4 carbon atoms. Suitable aryl groups include substituted or unsubstituted phenyl or naphthyl. The substituents of the substituted alkyl and aryl groups may be, for example, alkyl, halo and alkoxy.
- More specifically, suitable leveling agents include e.g. 1-(2-hydroxyethyl)-2-imidazolidinethione; 4-mercaptopyridine; 2-mercaptothiazoline; ethylene thiourea; thiourea; alkylated polyalkyleneimine; phenazonium compounds disclosed in U.S. Pat. No. 3,956,084; N-heteroaromatic rings containing polymers; quaternized, acrylic, polymeric amines; polyvinyl carbamates; pyrrolidone; and imidazole. A particularly preferred leveler is 1-(2-hydroxyethyl)-2-imidazolidinethione. Typical concentrations of leveling agents range from about 0.05 to 0.5 mg per liter of plating solution.
- The copper electroplating compositions are suitably used in similar manner as prior copper electroplating baths, except an elevated brightener concentration is employed and preferably maintained at an elevated level throughout a plating cycle.
- For instance, with reference to a printed circuit board substrate, a copper clad plastic substrate is typically employed, e.g. a copper clad glass fiber reinforced epoxy panel. Prior to formation of a circuit, apertures, such as microvias, are formed in the board by drilling and metallization. Microvias and other apertures also may be formed by photoimaging. Processes for forming such apertures in electronic device substrates are known and are disclosed e.g. in U.S. Pat. No. 4,902,610; C. Coombs,Printed Circuits Handbook, (4th ed., McGraw Hill); and T. Kiko, Printed Circuit Board Basics (PMS Indus.).
- After formation of the microvia or other aperture, electroless plating procedures are then used to form a first metallic coating over the substrate surfaces and electrolytic copper deposition is then used to enhance the thickness of the coating. Alternatively, electrolytic copper may be plated directly over a suitably prepared microvia as disclosed in any of U.S. Pat. Nos. 5,425,873; 5,207,888; and 4,919,768. The next step in the process comprises electroplating copper onto the thus prepared conductive microvias using an electroplating solution of the invention.
- Plating baths of the invention are preferably employed at or above room temperature, e.g. up to and somewhat above 65° C. The plating composition is preferably agitated during use such as by air sparger, work piece agitation, impingement or other suitable method. Plating is preferably conducted at a current ranging from 1 to 40 ASF depending upon substrate characteristics. Plating time may range from about 5 minutes to 1 hour or more, depending on the difficulty of the work piece. See generally the examples which follow for exemplary preferred procedures.
- A wide variety of substrates may be plated with the compositions of the invention, as discussed above. The compositions of the invention are particularly useful to plate difficult work pieces, such as circuit board substrates with small diameter, high aspect ratio microvias and other apertures. The plating compositions of the invention also will be particularly useful for plating integrated circuit devices, such as formed semiconductor devices and the like. See the examples which follow for exemplary substrates plated in accordance with the invention.
- As discussed above, aspect ratios of at least 4:1, having diameters of about 200 nm or smaller have been effectively copper plated with no defects (e.g. no voids or inclusions by ion beam examination) using plating solutions of the invention. Microvias with diameters below 150 nm, or even below about 100 nm, and aspect ratios of 5:1, 6:1, 7:1, 10:1 or greater, and even up to about 15:1 or greater can be effectively plated (e.g. no voids or inclusions by ion beam examination) using plating solutions of the invention.
- All documents mentioned herein are fully incorporated herein by reference. The following non-limiting examples are illustrative of the invention.
- A preferred copper electroplating bath of the invention was prepared by admixing the following components in water. In the composition the brightener was bis-sodium-sulfonopropyl-disulfide and the suppressor was a polyethylene glycol polymer sold under the tradename PEG 8000 by Union Carbide.
Component Concentration CuSO45H2O 60 g/l H2SO4 225 g/l Cl 50 ppm Suppressor 1 g/l Brightener 2.1 mg/l - Through hole walls of a printed circuit board substrate and microvias were plated as follows with the above plating composition. An air-agitated plating tank outfitted with multiple cathode rails and one rectifier was charged with the above copper plating solution. During plating, the following deposition conditions were employed:
- current density of 14.5 mA/cm2; waveform was DC; temperature plating bath was 25° C. After termination of the plating procedure, a microvia of the board substrate was examined. It was found that copper completely filled the microvia walls to provide a smooth uniform copper plate with no voids.
- A further preferred copper electroplating bath of the invention was prepared by admixing the following components in water. In the composition the brightener was bis-sodium-sulfonopropyl-disulfide and the suppressor was a propylene glycol copolymer sold under the tradename L62D by BASF.
Component Concentration CuSO45H2O 70 g/l H2SO4 175 g/l Cl 50 ppm Suppressor 0.875 g/l Brightener 2.4 mg/l - 200 nm with 7:1 aspect ratio microvias of a back end of the line semiconductor microchip wafer were plated using the above plating composition. The wafer was electrically attached to a cathode and the plating solution was pumped onto the surface of the wafer while rotating at upwards of 200 RPM. Electrical current of 14.5 mA/cm2 was applied with DC wave form at 25° C. After termination of the plating procedure, the microvias were filled with no defects as determined by focused ion beam examination.
- A further preferred copper electroplating bath of the invention was prepared by admixing the following components in water. In the composition the brightener was bis-sodium-sulfonopropyl-disulfide and the suppressor was a propylene glycol copolymer sold under the tradename L62D by BASF.
Component Concentration CuSO45H2O 60 g/l H2SO4 225 g/l Cl 50 ppm Suppressor 1 g/l Brightener 0.35 mg/l - 200 nm with 4:1 aspect ratio microvias of a semiconductor microchip wafer were plated using the above comparative plating composition under conditions as described in Example 2. After termination of the plating procedure, the microvias were examined by scanning electron microscopy (SEM) and focused ion beam examination. Those examinations showed the copper deposits in the microvias contained defects of voids, seams and inclusions.
- The foregoing description of the invention is merely illustrative thereof, and it is understood that variations and modifications can be effected without departing from the scope or spirit of the invention as set forth in the following claims.
Claims (23)
1. A copper electroplating composition comprising:
at least one soluble copper salt,
an electrolyte, and
one or more brightener compounds that are present in a concentration of at least about 1.5 mg per liter of the electroplating composition.
2. The composition of claim 1 wherein the concentration of the brightener agent is at least about 2 mg per liter of the electroplating composition.
3. The composition of claim 1 wherein the concentration of the brightener agent is at least about 4 mg per liter of the electroplating composition.
4. The composition of claim 1 wherein the concentration of the brightener agent is at least about 10 mg per liter of the electroplating composition.
5. The composition of claim 1 wherein the concentration of the brightener agent is at least about 25 mg per liter of the electroplating solution.
6. The composition of claim 1 wherein the one or more brightener compounds contain one or more sulfur atoms.
7. The composition of claim 1 wherein the one or more brightener compounds comprise one or more sulfide or sulfonic acid groups.
8. The composition of claim 1 wherein the one or more brightener compounds comprise a group of the formula R′—S—RSO3 where R is optionally substituted alkyl, optionally substituted heteroalkyl, optionally substituted aryl, optionally substituted heteroaromatic, or optionally substituted heteroalicyclic; and R′ is hydrogen or a chemical bond.
9. The composition of claim 1 wherein the composition further comprises a suppressor agent.
10. The composition of claim 9 wherein the suppressor agent is a polyether.
11. The composition of claim 1 wherein the composition further comprises a leveler agent.
12. The composition of claim 1 wherein the electroplating composition is acidic.
13. A method for plating an electronic device substrate containing one or more apertures, the method comprising:
electrolytically depositing onto the substrate copper from an electroplating composition that comprises at least one soluble copper salt, an electrolyte, and one or more brightener compounds that are present in a concentration of at least about 1.5 mg per liter of the electroplating composition.
14. The method of claim 13 wherein the brightener concentration is at least about 2 mg per liter of the electroplating solution.
15. The method of claim 13 wherein the brightener concentration is at least about 10 mg per liter of the electroplating solution.
16. The method of claim 13 wherein the substrate is a printed circuit board substrate or semiconductor with one or microvias.
17. The method of claim 16 wherein the one or more microvias have an aspect ratio of at least about 4:1 and diameters of at least about 200 nm.
18. The method of claim 17 wherein copper is deposited to fill the one or more microvias to provide a copper plate in the absence of voids or inclusions.
19. The method of claim 17 wherein the composition further comprises a suppressor agent.
20. The method of claim 13 wherein the substrate is a microchip module substrate.
21. An article of manufacture comprising an electronic device substrate containing one or more apertures each having walls, the aperture walls having thereon an electrolytic copper deposit obtained from an electroplating composition that comprises at least one soluble copper salt, an electrolyte, and one or more brightener compounds that are present in a concentration of at least about 1.5 mg per liter of the electroplating composition.
22. The article of claim 21 wherein the substrate is printed board substrate, a microchip module substrate, or a semiconductor chip substrate.
23. The article of claim 21 wherein the substrate comprises the one or more microvias that have an aspect ratio of at least about 4:1 and diameters of at least about 200 nm, and the walls of the one or more microvias have a copper deposit that is free of voids.
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US10/225,677 US20030010646A1 (en) | 1999-05-17 | 2002-08-22 | Electrolytic copper plating solutions |
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Citations (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2424887A (en) * | 1941-10-11 | 1947-07-29 | Houdaille Hershey Corp | Method and electrolyte for the electrodeposition of metals |
US3674660A (en) * | 1967-05-01 | 1972-07-04 | Albright & Wilson | Electrodeposition of copper |
US3770598A (en) * | 1972-01-21 | 1973-11-06 | Oxy Metal Finishing Corp | Electrodeposition of copper from acid baths |
US3778357A (en) * | 1972-01-26 | 1973-12-11 | Schering Ag | Electrolyte and method for electrodepositing copper |
US3876513A (en) * | 1972-06-26 | 1975-04-08 | Oxy Metal Finishing Corp | Electrodeposition of bright cobalt plate |
US4036710A (en) * | 1974-11-21 | 1977-07-19 | M & T Chemicals Inc. | Electrodeposition of copper |
US4098656A (en) * | 1976-03-11 | 1978-07-04 | Oxy Metal Industries Corporation | Bright palladium electroplating baths |
US4336114A (en) * | 1981-03-26 | 1982-06-22 | Hooker Chemicals & Plastics Corp. | Electrodeposition of bright copper |
US4347108A (en) * | 1981-05-29 | 1982-08-31 | Rohco, Inc. | Electrodeposition of copper, acidic copper electroplating baths and additives therefor |
US4530741A (en) * | 1984-07-12 | 1985-07-23 | Columbia Chemical Corporation | Aqueous acid plating bath and brightener composition for producing bright electrodeposits of tin |
US4913787A (en) * | 1988-09-06 | 1990-04-03 | C. Uyemura & Co., Ltd. | Gold plating bath and method |
US5051154A (en) * | 1988-08-23 | 1991-09-24 | Shipley Company Inc. | Additive for acid-copper electroplating baths to increase throwing power |
US5068013A (en) * | 1988-08-23 | 1991-11-26 | Shipley Company Inc. | Electroplating composition and process |
US5151170A (en) * | 1991-12-19 | 1992-09-29 | Mcgean-Rohco, Inc. | Acid copper electroplating bath containing brightening additive |
US5174886A (en) * | 1991-02-22 | 1992-12-29 | Mcgean-Rohco, Inc. | High-throw acid copper plating using inert electrolyte |
US5223118A (en) * | 1991-03-08 | 1993-06-29 | Shipley Company Inc. | Method for analyzing organic additives in an electroplating bath |
US5252196A (en) * | 1991-12-05 | 1993-10-12 | Shipley Company Inc. | Copper electroplating solutions and processes |
US5433840A (en) * | 1991-08-07 | 1995-07-18 | Atotech Deutschland Gmbh | Acid bath for the galvanic deposition of copper, and the use of such a bath |
US5858870A (en) * | 1996-12-16 | 1999-01-12 | Chartered Semiconductor Manufacturing, Ltd. | Methods for gap fill and planarization of intermetal dielectrics |
US5972192A (en) * | 1997-07-23 | 1999-10-26 | Advanced Micro Devices, Inc. | Pulse electroplating copper or copper alloys |
US6024857A (en) * | 1997-10-08 | 2000-02-15 | Novellus Systems, Inc. | Electroplating additive for filling sub-micron features |
US6113771A (en) * | 1998-04-21 | 2000-09-05 | Applied Materials, Inc. | Electro deposition chemistry |
US6117784A (en) * | 1997-11-12 | 2000-09-12 | International Business Machines Corporation | Process for integrated circuit wiring |
US6709562B1 (en) * | 1995-12-29 | 2004-03-23 | International Business Machines Corporation | Method of making electroplated interconnection structures on integrated circuit chips |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2039831C3 (en) * | 1970-06-06 | 1979-09-06 | Schering Ag, 1000 Berlin Und 4619 Bergkamen | Acid bath for the galvanic deposition of shiny copper coatings |
US4272335A (en) * | 1980-02-19 | 1981-06-09 | Oxy Metal Industries Corporation | Composition and method for electrodeposition of copper |
DD159268A3 (en) * | 1980-10-23 | 1983-03-02 | Eberhard Wuensche | PROCESS FOR THE GALVANIC DEPOSITION OF COPPER LAYERS ON PCB |
US4555315A (en) * | 1984-05-29 | 1985-11-26 | Omi International Corporation | High speed copper electroplating process and bath therefor |
US4673469A (en) * | 1984-06-08 | 1987-06-16 | Mcgean-Rohco, Inc. | Method of plating plastics |
DE3836521C2 (en) * | 1988-10-24 | 1995-04-13 | Atotech Deutschland Gmbh | Aqueous acidic bath for the galvanic deposition of shiny and crack-free copper coatings and use of the bath |
US5882251A (en) * | 1997-08-19 | 1999-03-16 | Lsi Logic Corporation | Chemical mechanical polishing pad slurry distribution grooves |
WO2000014306A1 (en) * | 1998-09-03 | 2000-03-16 | Ebara Corporation | Method for plating substrate and apparatus |
-
1999
- 1999-05-17 US US09/313,045 patent/US6444110B2/en not_active Expired - Lifetime
-
2000
- 2000-03-30 SG SG200001790A patent/SG93233A1/en unknown
- 2000-05-15 TW TW089109219A patent/TWI245816B/en not_active IP Right Cessation
- 2000-05-15 EP EP00304093.8A patent/EP1054080B1/en not_active Expired - Lifetime
- 2000-05-15 KR KR10-2000-0025736A patent/KR100514251B1/en not_active Expired - Lifetime
- 2000-05-16 CN CNB001085506A patent/CN1260398C/en not_active Expired - Lifetime
- 2000-05-17 JP JP2000144780A patent/JP2001003191A/en active Pending
-
2002
- 2002-08-22 US US10/225,677 patent/US20030010646A1/en not_active Abandoned
-
2005
- 2005-08-17 US US11/207,172 patent/US20060065537A1/en not_active Abandoned
Patent Citations (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2424887A (en) * | 1941-10-11 | 1947-07-29 | Houdaille Hershey Corp | Method and electrolyte for the electrodeposition of metals |
US3674660A (en) * | 1967-05-01 | 1972-07-04 | Albright & Wilson | Electrodeposition of copper |
US3784454A (en) * | 1967-05-01 | 1974-01-08 | Albright & Wilson | Additive for the electrodeposition of copper |
US3770598A (en) * | 1972-01-21 | 1973-11-06 | Oxy Metal Finishing Corp | Electrodeposition of copper from acid baths |
US3778357A (en) * | 1972-01-26 | 1973-12-11 | Schering Ag | Electrolyte and method for electrodepositing copper |
US3876513A (en) * | 1972-06-26 | 1975-04-08 | Oxy Metal Finishing Corp | Electrodeposition of bright cobalt plate |
US4036710A (en) * | 1974-11-21 | 1977-07-19 | M & T Chemicals Inc. | Electrodeposition of copper |
US4098656A (en) * | 1976-03-11 | 1978-07-04 | Oxy Metal Industries Corporation | Bright palladium electroplating baths |
US4336114A (en) * | 1981-03-26 | 1982-06-22 | Hooker Chemicals & Plastics Corp. | Electrodeposition of bright copper |
US4347108A (en) * | 1981-05-29 | 1982-08-31 | Rohco, Inc. | Electrodeposition of copper, acidic copper electroplating baths and additives therefor |
US4530741A (en) * | 1984-07-12 | 1985-07-23 | Columbia Chemical Corporation | Aqueous acid plating bath and brightener composition for producing bright electrodeposits of tin |
US5051154A (en) * | 1988-08-23 | 1991-09-24 | Shipley Company Inc. | Additive for acid-copper electroplating baths to increase throwing power |
US5068013A (en) * | 1988-08-23 | 1991-11-26 | Shipley Company Inc. | Electroplating composition and process |
US4913787A (en) * | 1988-09-06 | 1990-04-03 | C. Uyemura & Co., Ltd. | Gold plating bath and method |
US5174886A (en) * | 1991-02-22 | 1992-12-29 | Mcgean-Rohco, Inc. | High-throw acid copper plating using inert electrolyte |
US5223118A (en) * | 1991-03-08 | 1993-06-29 | Shipley Company Inc. | Method for analyzing organic additives in an electroplating bath |
US5433840A (en) * | 1991-08-07 | 1995-07-18 | Atotech Deutschland Gmbh | Acid bath for the galvanic deposition of copper, and the use of such a bath |
US5252196A (en) * | 1991-12-05 | 1993-10-12 | Shipley Company Inc. | Copper electroplating solutions and processes |
US5151170A (en) * | 1991-12-19 | 1992-09-29 | Mcgean-Rohco, Inc. | Acid copper electroplating bath containing brightening additive |
US6709562B1 (en) * | 1995-12-29 | 2004-03-23 | International Business Machines Corporation | Method of making electroplated interconnection structures on integrated circuit chips |
US5858870A (en) * | 1996-12-16 | 1999-01-12 | Chartered Semiconductor Manufacturing, Ltd. | Methods for gap fill and planarization of intermetal dielectrics |
US5972192A (en) * | 1997-07-23 | 1999-10-26 | Advanced Micro Devices, Inc. | Pulse electroplating copper or copper alloys |
US6024857A (en) * | 1997-10-08 | 2000-02-15 | Novellus Systems, Inc. | Electroplating additive for filling sub-micron features |
US6117784A (en) * | 1997-11-12 | 2000-09-12 | International Business Machines Corporation | Process for integrated circuit wiring |
US6113771A (en) * | 1998-04-21 | 2000-09-05 | Applied Materials, Inc. | Electro deposition chemistry |
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US7510639B2 (en) | 2004-07-22 | 2009-03-31 | Rohm And Haas Electronic Materials Llc | Leveler compounds |
US20060016693A1 (en) * | 2004-07-22 | 2006-01-26 | Rohm And Haas Electronic Materials Llc | Leveler compounds |
US20070012576A1 (en) * | 2005-07-13 | 2007-01-18 | Rohm And Haas Electronic Materials Llc | Plating method |
US7662981B2 (en) | 2005-07-16 | 2010-02-16 | Rohm And Haas Electronic Materials Llc | Leveler compounds |
US20090139873A1 (en) * | 2005-07-16 | 2009-06-04 | Rohm And Haas Electronic Materials Llc | Leveler compounds |
WO2007126453A3 (en) * | 2006-04-05 | 2007-12-21 | Macdermid Inc | Process for electrolytically plating copper |
US7575666B2 (en) * | 2006-04-05 | 2009-08-18 | James Watkowski | Process for electrolytically plating copper |
US20070235343A1 (en) * | 2006-04-05 | 2007-10-11 | James Watkowski | Process for electrolytically plating copper |
US20090090631A1 (en) * | 2007-10-03 | 2009-04-09 | Emat Technology, Llc | Substrate holder and electroplating system |
US7905994B2 (en) | 2007-10-03 | 2011-03-15 | Moses Lake Industries, Inc. | Substrate holder and electroplating system |
US20090188553A1 (en) * | 2008-01-25 | 2009-07-30 | Emat Technology, Llc | Methods of fabricating solar-cell structures and resulting solar-cell structures |
US8262894B2 (en) | 2009-04-30 | 2012-09-11 | Moses Lake Industries, Inc. | High speed copper plating bath |
CN106521573A (en) * | 2016-11-23 | 2017-03-22 | 苏州昕皓新材料科技有限公司 | Method for producing electroplated copper layer with preferential orientation growth structure, and application thereof |
CN106757191A (en) * | 2016-11-23 | 2017-05-31 | 苏州昕皓新材料科技有限公司 | A kind of copper crystal particle with preferred orientation high and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
KR20000077270A (en) | 2000-12-26 |
TWI245816B (en) | 2005-12-21 |
KR100514251B1 (en) | 2005-09-13 |
CN1274021A (en) | 2000-11-22 |
EP1054080A2 (en) | 2000-11-22 |
US20060065537A1 (en) | 2006-03-30 |
US6444110B2 (en) | 2002-09-03 |
US20010047943A1 (en) | 2001-12-06 |
JP2001003191A (en) | 2001-01-09 |
EP1054080A3 (en) | 2004-03-03 |
EP1054080B1 (en) | 2017-04-12 |
CN1260398C (en) | 2006-06-21 |
SG93233A1 (en) | 2002-12-17 |
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