JP3739929B2 - Copper foil for printed wiring board and method for producing the same - Google Patents

Copper foil for printed wiring board and method for producing the same Download PDF

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JP3739929B2
JP3739929B2 JP05652198A JP5652198A JP3739929B2 JP 3739929 B2 JP3739929 B2 JP 3739929B2 JP 05652198 A JP05652198 A JP 05652198A JP 5652198 A JP5652198 A JP 5652198A JP 3739929 B2 JP3739929 B2 JP 3739929B2
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plating layer
copper
copper foil
printed wiring
nickel
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JPH11256389A (en
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昭利 鈴木
伸 福田
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古河サーキットフォイル株式会社
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Description

【0001】
【発明の属する技術分野】
本発明は、プリント配線板用銅箔及びその製造方法に関する。
【0002】
【従来の技術】
プリント配線板用銅箔は、それを基材に接合させるにあたり、その、接着強度を向上させ、プリント配線板としての所要の電気特性、エッチング特性、耐熱性、耐薬品性を満足させるために、該銅箔の被接合面に粗化処理を施し、更には該粗化処理を施された面上に亜鉛めっきやニッケルめっき等を施し、また更には該亜鉛めっきやニッケルめっき等を施された面上にクロメート処理等を施す等、種々工夫されている。
【0003】
最近多用されているそれらの具体的方法としては、下記のものが挙げられる。
【0004】
▲1▼ 特公昭40−15327号に開示された方法
酸性銅電解浴中で銅箔を陰極とし、限界電流密度付近で電解を行うことにより、いわゆる「やけめっき」を施して粗化面を得る方法である。
【0005】
▲2▼ 米国特許第3293109号に開示された方法
「やけめっき」を施された粗化面の微細な突起群の表面を通常の銅めっきの薄層(いわゆる「カプセル層」)で覆って、該粗化面の微細な突起群を銅箔の安定的に固定する方法。
【0006】
▲3▼ 特公昭54−38053号に開示された方法
比較的粗大な樹枝状突起の生成を防止し、より微細で且つ全面が均一な突起群よりなる粗化面を得るために、酸性銅電解浴の電解液中にセレン、テルル、ヒ素、アンチモン、ビスマスの少なくとも1種を0.01〜1g-M/l (M = Se, Te, As, Sb, Bi)に添加する方法。
【0007】
▲4▼ 特公昭53−39327号に開示された方法
セレン、テルル、ヒ素、アンチモン、ビスマスの少なくとも1種を0.03〜5g-M/l (M = Se, Te, As, Sb, Bi)添加した電解液を含む酸性銅電解浴にて「やけめっき」を施し、形成された微細な樹枝状突起群の表面を通常の銅めっきの薄層で覆って該突起群の脱落を防止し粉状移着特性を改善すると共に基材に対する接着強度を改善せんとした方法。
【0008】
しかしながら、セレン、テルル、ヒ素、アンチモン、ビスマスを含む化合物は、毒物、劇物、もしくはこれらに類するものとされているものが多く、電解時にこれらの元素が銅電着物中に取り込まれる結果、銅箔やそれを用いたプリント配線板の再生時や廃棄時、またこれらの元素を含有することになるエッチング廃液の処分時に、環境への汚染に対し最大限の注意が必要である。更に、毒性の弱いものは、これらの元素を添加することによって得られる効果が小さい。
【0009】
一方、その中にこれらの金属を含まない電解液を用いたもの、すなわち銅のみの「やけめっき層」を形成したものは、たとえ「やけめっき層」の上に更に通常の銅めっき層を形成したとしても「やけめっき層」の微細突起自体が粗雑なものとなり、また該微細突起群は不均一である。このような「やけめっき層」を有する銅箔の被接着面の表面を摩擦するとかなりの量の微細銅粉が剥落し、また樹脂基板と重ねて銅貼り積層板としたものはエッチングを行った後該基板表面に銅粉が残留する等の欠点を有していた。
【0010】
これらの欠点を改良するものとして、a.ベンゾキノリン類を添加した電解液を用いて粗化処理を行う方法(特公昭56−44196号公報);b.モリブデン及び/又はバナジウムを添加した電解液を用いて粗化処理を行う方法(特公昭62−56677号公報);c.パルス電流を粗化処理のための電解浴に供給する方法(特開昭58−16479号公報や特開昭63−17597号公報);が提唱されているが、いずれの方法も前記の毒性の強い元素の化合物を含む電解液を用いた粗化処理にて得られる銅箔に比し、剥離強度、粉落ち等の点で劣るものしか得られなかった。
【0011】
【発明が解決しようとする課題】
本発明は、従来の技術の課題を解決するためになされたものであって、基板への接着面表面が均質でムラがなく、粉落ちの点で問題がなく、基板との間で充分な接着強度を有し、耐熱性あるいは電気特性においても優れたプリント配線板用銅箔及びその製造方法を提供することを目的とする。
【0012】
【課題を解決するための手段】
本発明は、プリント配線板用銅箔であって、原銅箔の被接着面側表面に、やけめっき金属元素が、モリブデンと、鉄、コバルト、ニッケルの内の少なくとも1種と、からなる銅の「やけめっき層」を有することを特徴とする。
【0013】
ここで、前記の「やけめっき層」の膜厚(見かけ膜厚)は、0.2〜2.5μm であることが好ましく、0.4〜1.5μm であることが更に好ましい。ここで、「見かけ膜厚」とは、“やけめっき”の処理電流を流した時に電析する粒状のめっきを平滑めっきに換算して求めた膜厚である。
【0014】
本発明の銅箔は、前記の「やけめっき層」の上に「銅のめっき層」(いわゆる「カプセル層」)を更に有するものであってもよい。
【0015】
ここで、前記の「カプセル層」の膜厚(見かけ膜厚)は、0.2〜2.5μm であることが好ましく、0.4〜1.5μm であることが更に好ましい。
【0016】
尚、本発明の銅箔は、所望により、更に前記の「やけめっき層」又は「カプセル層」の上に、「ニッケルめっき層」又は「亜鉛めっき層」若しくは「ニッケルめっき層」と「亜鉛めっき層」を形成せしめたものであってもよい。また、本発明の銅箔は、所望により、クロメート皮膜を、更に前記の「カプセル層」の上に、或いは更に前記の「ニッケルめっき層」、「亜鉛めっき層」若しくは「ニッケルめっき層」と「亜鉛めっき層」の上に、形成せしめたものであってもよい。
【0017】
一方、本発明の銅箔の製造方法は、酸性銅電解浴を用い、被処理銅箔を陰極とし、該浴の限界電流密度付近の電流密度で電解して該銅箔表面に銅の「やけめっき層」を形成するプリント配線板用銅箔の製造方法であって、該浴の電解液中に、溶液の形態での、銅のやけめっき層のやけめっき金属元素が、モリブデンの0.001〜5g/lと、鉄、コバルト、ニッケルの少なくとも1種の0.01〜10g/lと、からなることを特徴とする。
【0018】
ここで、モリブデン濃度が0.001g/l未満では所望の効果が顕著ではないし、一方5g/l超でも所望の効果がその存在量の増加に比し顕著に増大しないので経済的ではなく、更に「やけめっき層」が粉状化しやすくなるので好ましくない。鉄、コバルト、ニッケルの規定濃度外の挙動もモリブデンのそれと同様である。尚、これらの添加剤の形態は電解液に溶解するものであれば特に限定されない(ただし、これらのハロゲン化物も殆どのものが電解液に溶解するが、粗化処理に悪影響を及ぼすので好ましくない)が、代表的な化合物としては下記のものが挙げられる。
1.モリブデン :モリブデン酸ナトリウム(2水塩)
2.鉄 :硫酸第1鉄(7水塩)
3.コバルト :硫酸コバルト(7水塩)
4.ニッケル :硫酸ニッケル(7水塩)
【0019】
酸性銅電解浴としては、鉱酸であればいずれの酸でも使用し得るが、通常は、硫酸浴(銅として硫酸銅含有)を用いる。
【0020】
硫酸銅−硫酸浴の液組成、液温は広い範囲で選択可能であるが、それらによって浴の限界電流密度はそれぞれの値を示すので、使用する電流密度は、液組成や液温、さらには液の動きなどで異なり、また「やけめっき」だけを施すのか、それとも更にその上に通常の銅めっき又は亜鉛めっき若しくはニッケルめっき等をカプセル上に施すのか、によっても異なるため、多少、電流密度を加減する必要がある。
【0021】
工業的にもちいられるのに好適な酸性銅電解浴の液条件を例示すると下記の通りである。
1.銅 :5〜50g/l
2.モリブデン:0.001〜5g/l
3.その他 :0.01〜10g/l
4.酸 :10〜100g-H2SO4/l
5.液温 :室温〜50℃
【0022】
更に、浴の循環量も特に限定されないが、浴成分の消耗分を補給する程度を下限とし、陰極表面近傍領域が著しい乱流域とならぬ程度を上限とし、その間で適宜選択するのが好ましい。
【0023】
また、処理時間は、数秒乃至数十秒の範囲が実際的で好ましいので、この程度の時間で所望の微細突起群が完成するよう、液組成や電流密度等の操作条件を設定するのがよい。
【0024】
本発明の銅箔の製造方法においては、前記の「やけめっき層」を形成する工程に次いで、該「やけめっき層」の上に「銅のめっき層」又は「ニッケルめっき層」、「亜鉛めっき層」若しくは「ニッケルめっき層」と「亜鉛めっき層」を形成する工程を行ってもよいし、所望により、更に該「銅のめっき層」形成工程に次いで、該「銅のめっき層」の上に「ニッケルめっき層」又は「亜鉛めっき層」若しくは「ニッケルめっき層」と「亜鉛めっき層」を形成する工程を行ってもよいし、更にまた該「銅のめっき層」形成工程又は該「ニッケルめっき層」形成工程、「亜鉛めっき層」形成工程若しくは「ニッケルめっき層」と「亜鉛めっき層」形成工程に次いで、該「銅のめっき層」又は該「ニッケルめっき層」、「亜鉛めっき層」若しくは「ニッケルめっき層」と「亜鉛めっき層」の上にクロメート皮膜を形成する工程を行ってもよい。これら追加工程の条件は、公知の方法のそれに従えばよい。
【0025】
尚、本発明の製造方法における被処理銅箔は、電解銅箔であってもよいし、また圧延銅箔であってもよい。本発明の方法では、銅箔の種類を選ばないからである。
【0026】
【発明の実施の形態】
以下に、本発明を実施例に基づいて更に詳しく説明する。但し、本発明はこれらに限定されるものではない。
【0027】
実施例1
(1)被処理銅箔(原銅箔)
電解銅箔(未処理銅箔;厚さ:18μm ;マット面の粗さ:Ra=0.6μm ;Rz=4.2μm ;古河サーキットフォイル(株)製)
(2)やけめっき層の形成
原銅箔に下記の条件にて直流による陰極電解処理を施し、該原銅箔のマット面上に微細な突起群からなる「やけめっき層」を電析させた。
▲1▼ 電解液の組成
・硫酸銅 :100g-CuSO4・5H2O/l
・硫酸 :120g-H2SO4/l
・モリブデン:0.6g-Na2MoO4・2H2O/l
・鉄 :15g-FeSO4・7H2O/l
▲2▼ 電解液の温度:35℃
▲3▼ 電流密度 :40A/dm2
▲4▼ 処理時間 :3.5sec.
(3)カプセルめっき
マット面上に微細な突起群が形成された前記の原銅箔に下記の条件にて直流による陰極電解処理を施し、該微細な突起群を銅の薄層で覆った。
▲1▼ 電解液の組成
・硫酸銅 :250g-CuSO4・5H2O/l
・硫酸 :100g-H2SO4/l
▲2▼ 電解液の温度:50℃
▲3▼ 電流密度 :20A/dm2
▲4▼ 処理時間 :7.0sec.
(4)更に前記の(2)→(3)の処理をもう一度繰り返した。
(5)表面処理
得られた銅箔(以下、「粗化処理銅箔」という)の被接合面側の表面に、ニッケル−リンめっき(0.1mg/dm2)と亜鉛めっき(0.1mg/dm2)を施し、更にその上にクロメート処理を施した試料(以下、「表面処理銅箔」という)を作成した。
【0028】
得られた表面処理銅箔の特性を下記の項目についてそれぞれ評価した。
【0029】
(1)ピール強度
得られた表面処理銅箔をFR−4基材にプレスし接着したものを試料とし、JIS C 6481 「プリント配線板用銅貼積層板試験方法」の5.7に従って常態ピール(常態での「引きはがし強さ」)を測定した。
【0030】
(2)耐塩酸劣化率
得られた表面処理銅箔をFR−4基材にプレスし接着した後、該表面処理銅箔を1mm幅にエッチングしたものを試料とし、JIS C 6481 「プリント配線板用銅貼積層板試験方法」の5.7に従って常態ピールと劣化処理後のピール(35%塩酸と蒸留水を同量混合した25℃の処理液に該試料を 1時間浸漬したものの「引きはがし強さ」。以下、「劣化後ピール」という)を測定し、下記の式に従って計算にて求めた。
耐塩酸劣化率(%)=(1−(劣化後ピール/常態ピール))×100
【0031】
(3)粉落ち
得られた表面処理銅箔上に試験紙(東洋ろ紙No. 2)を置き、それに荷重(250g/20mmφ)をかけたまま該試験紙を150mm水平方向に引きずった。該試験紙に付着する銅粉を目視観察し、付着量に応じてA<B<C<D<E<Fの順に評価付けした(A:粉落ち“ゼロ”、F:粉落ちが最も多い)。
【0032】
結果を表1に示す。
【0033】
例2
処理(2)における電解液の組成を下記のものに代えたことを除き実施例1と同様にして粗化処理銅箔及び表面処理銅箔をそれぞれ作製し、該表面処理銅箔について実施例1と同様の特性評価を行った。結果を表1に示す。
<1> 電解液の組成
・硫酸銅 :100g-CuSO4・5H2O/l
・硫酸 :120g-H2SO4/l
・モリブデン :0.05g-Na2MoO4・2H2O/l
・タングステン:0.05g-Na2WO4・2H2O/l
【0034】
例3
処理(2)における電解液の組成を下記のものに代えたことを除き実施例1と同様にして粗化処理銅箔及び表面処理銅箔をそれぞれ作製し、該表面処理銅箔について実施例1と同様の特性評価を行った。結果を表1に示す。
<1> 電解液の組成
・硫酸銅 :100g-CuSO4・5H2O/l
・硫酸 :120g-H2SO4/l
・モリブデン :0.6g-Na2MoO4・2H2O/l
・鉄 :15g-FeSO4・7H2O/l
・タングステン:0.03g-Na2WO4・2H2O/l
【0035】
実施例4
処理(2)における電解液の組成を下記のものに代えたことを除き実施例1と同様にして粗化処理銅箔及び表面処理銅箔をそれぞれ作製し、該表面処理銅箔について実施例1と同様の特性評価を行った。結果を表1に示す。
▲1▼ 電解液の組成
・硫酸銅 :100g-CuSO4・5H2O/l
・硫酸 :120g-H2SO4/l
・モリブデン:0.6g-Na2MoO4・2H2O/l
・コバルト :10g-CoSO4・7H2O/l
【0036】
実施例5
処理(2)における電解液の組成を下記のものに代えたことを除き実施例1と同様にして粗化処理銅箔及び表面処理銅箔をそれぞれ作製し、該表面処理銅箔について実施例1と同様の特性評価を行った。結果を表1に示す。
▲1▼ 電解液の組成
・硫酸銅 :100g-CuSO4・5H2O/l
・硫酸 :120g-H2SO4/l
・モリブデン:0.6g-Na2MoO4・2H2O/l
・ニッケル :10g-NiSO4・7H2O/l
【0037】
比較例1
処理(2)における電解液の組成を下記のものに代えたことを除き実施例1と同様にして粗化処理銅箔及び表面処理銅箔をそれぞれ作製し、該表面処理銅箔について実施例1と同様の特性評価を行った。結果を表1に示す。
▲1▼ 電解液の組成
・硫酸銅 :100g-CuSO4・5H2O/l
・硫酸 :120g-H2SO4/l
・ヒ素 :0.4cc/l as 60% H3AsO4(比重:1.58)
【0038】
比較例2
処理(2)における電解液の組成を下記のものに代えたことを除き実施例1と同様にして粗化処理銅箔及び表面処理銅箔をそれぞれ作製し、該表面処理銅箔について実施例1と同様の特性評価を行った。結果を表1に示す。
▲1▼ 電解液の組成
・硫酸銅 :100g-CuSO4・5H2O/l
・硫酸 :120g-H2SO4/l
・モリブデン:0.6g-Na2MoO4・2H2O/l
【0039】
実施例1、4、5、例2、3及び比較例1〜2にて得られた各粗化処理銅箔の粗化処理を施した面を硫酸−過酸化水素のソフトエッチング液(H2SO4: 100g/l 、H2O2: 30g/l 、n−プロパノール:10cc/l)に1分間浸漬して該粗化処理被膜を溶解し、該溶解液を蒸発乾固して該溶解液中に含まれる過酸化水素を分解除去した後、原子吸光分析法(日立(株)Z-6100形偏光ゼーマン原子吸光分光光度計を使用)にて該溶解液中の対象元素の定量分析を行った。その結果を表2に示す。尚、データは該粗化処理被膜中の存在量に換算したものである。
【0040】
【表1】

Figure 0003739929
【0041】
【表2】
Figure 0003739929
【0042】
【発明の効果】
表1に示す通り、本発明の銅箔は、ピール強度、耐塩酸劣化率、粉落ち共毒性の強いヒ素を用いたもの(従来技術の一つ)と遜色ない性能を有するものである。これに対し、従来技術の他例(毒物を含まない)として挙げたモリブデン単用の銅箔は、ピール強度が低く、粉落ちも多く実用上問題の大きいものであることがわかる。
すなわち本発明に従えば、プリント配線板用銅箔としての所定の性能を充分に満足する環境に優しい銅箔及びそのための製造方法を提供することができる。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a copper foil for printed wiring boards and a method for producing the same.
[0002]
[Prior art]
In order to join the copper foil for printed wiring board to the base material, the adhesive strength is improved, and in order to satisfy the required electrical characteristics, etching characteristics, heat resistance, chemical resistance as a printed wiring board, The surface of the copper foil to be joined was subjected to a roughening treatment, and further, the surface subjected to the roughening treatment was subjected to galvanization or nickel plating, and further, the galvanization or nickel plating was performed. Various devices have been devised, such as chromate treatment on the surface.
[0003]
Specific examples of these methods that are frequently used recently include the following.
[0004]
(1 ) Method disclosed in Japanese Examined Patent Publication No. 40-15327 A copper foil is used as a cathode in an acidic copper electrolytic bath, and electrolysis is performed in the vicinity of the limiting current density, so-called "bake plating" is applied to roughen the surface. This is a method for obtaining a chemical surface.
[0005]
(2) Covering the surface of the fine protrusions on the roughened surface subjected to the methodbake plating” disclosed in US Pat. No. 3,293,109 with a thin layer of copper (so-called “capsule layer”), A method of stably fixing a fine projection group on the roughened surface of a copper foil.
[0006]
(3 ) Method disclosed in Japanese Examined Patent Publication No. 54-38053 In order to prevent the formation of relatively coarse dendritic protrusions and to obtain a roughened surface comprising a group of protrusions that are finer and uniform on the entire surface. A method of adding at least one of selenium, tellurium, arsenic, antimony, and bismuth to 0.01 to 1 g-M / l (M = Se, Te, As, Sb, Bi) in an electrolytic solution of an acidic copper electrolytic bath .
[0007]
(4 ) Method disclosed in JP-B-53-39327 At least one of selenium, tellurium, arsenic, antimony and bismuth is added in an amount of 0.03 to 5 g-M / l (M = Se, Te, As, "Sb, Bi)" Bake plating "is performed in an acidic copper electrolytic bath containing the added electrolyte, and the surface of the formed fine dendritic protrusions is covered with a thin layer of ordinary copper plating, and the protrusions are removed. Is a method to improve the adhesion strength to the base material while preventing powder and improving the powder transfer characteristics.
[0008]
However, many compounds containing selenium, tellurium, arsenic, antimony and bismuth are considered to be poisonous, deleterious, or similar, and as a result of these elements being incorporated into the electrodeposited copper during electrolysis, When reclaiming or discarding a foil or a printed wiring board using the same, or when disposing of an etching waste solution containing these elements, utmost care must be taken against environmental pollution. Furthermore, the effect obtained by adding these elements is small for those having low toxicity.
[0009]
On the other hand, those using electrolytes that do not contain these metals, that is, those that have a “bake plating layer” made only of copper, even if a normal copper plating layer is formed on the “bake plating layer” Even so, the fine protrusions themselves of the “bake plating layer” are rough, and the fine protrusion groups are not uniform. When rubbing the surface of the adherend surface of the copper foil having such a “bake plating layer”, a considerable amount of fine copper powder is peeled off, and the copper-clad laminate laminated with the resin substrate is etched. Later, there were defects such as copper powder remaining on the surface of the substrate.
[0010]
Improvements to these drawbacks include: a. A method of performing a roughening treatment using an electrolytic solution to which benzoquinolines are added (Japanese Patent Publication No. 56-44196); b. A method of performing a roughening treatment using an electrolytic solution to which molybdenum and / or vanadium is added (Japanese Patent Publication No. Sho 62-56777); c. A method of supplying a pulse current to an electrolytic bath for roughening treatment (Japanese Patent Laid-Open Nos. 58-16479 and 63-17597) has been proposed. As compared with the copper foil obtained by the roughening treatment using the electrolytic solution containing a strong elemental compound, only inferior ones in terms of peel strength, powder fall, and the like were obtained.
[0011]
[Problems to be solved by the invention]
The present invention has been made in order to solve the problems of the prior art, the surface of the adhesion surface to the substrate is uniform and non-uniform, there is no problem in terms of powder falling, and sufficient between the substrate and the substrate An object of the present invention is to provide a copper foil for a printed wiring board having adhesive strength and excellent in heat resistance or electrical characteristics, and a method for producing the same.
[0012]
[Means for Solving the Problems]
The present invention is a copper foil for a printed wiring board, and a copper plating metal element on the surface to be bonded of the original copper foil is made of molybdenum and at least one of iron, cobalt, and nickel. It is characterized by having a “burnt plating layer”.
[0013]
Here, the film thickness (apparent film thickness) of the “burnt plating layer” is preferably 0.2 to 2.5 μm, and more preferably 0.4 to 1.5 μm. Here, the “apparent film thickness” is a film thickness obtained by converting a granular plating electrodeposited when a “burn plating” treatment current is passed into a smooth plating.
[0014]
The copper foil of the present invention may further have a “copper plating layer” (so-called “capsule layer”) on the “bake plating layer”.
[0015]
Here, the film thickness (apparent film thickness) of the “capsule layer” is preferably 0.2 to 2.5 μm, and more preferably 0.4 to 1.5 μm.
[0016]
In addition, the copper foil of the present invention may be further provided with a “nickel plating layer” or “zinc plating layer” or “nickel plating layer” and “zinc plating” on the above “bake plating layer” or “capsule layer”. A layer "may be formed. In addition, the copper foil of the present invention may further comprise a chromate film on the “capsule layer” or further on the “nickel plating layer”, “zinc plating layer” or “nickel plating layer”, if desired. It may be formed on the “galvanized layer”.
[0017]
On the other hand, the method for producing a copper foil of the present invention uses an acidic copper electrolytic bath, uses the copper foil to be treated as a cathode, electrolyzes at a current density in the vicinity of the limit current density of the bath, and performs a copper burn on A method for producing a copper foil for a printed wiring board for forming a “plating layer”, wherein the burnt plating metal element of the copper burnt plating layer in the form of a solution is 0.001 of molybdenum in the electrolytic solution of the bath. ˜5 g / l and 0.01 to 10 g / l of at least one of iron, cobalt and nickel.
[0018]
Here, if the molybdenum concentration is less than 0.001 g / l, the desired effect is not remarkable. On the other hand, if the molybdenum concentration exceeds 5 g / l, the desired effect does not increase remarkably as compared with the increase in the abundance, so that it is not economical. The “bake plating layer” is not preferable because it is easily powdered. The behavior of iron, cobalt, and nickel outside the specified concentration is the same as that of molybdenum. The form of these additives is not particularly limited as long as it is soluble in the electrolytic solution (although most of these halides are dissolved in the electrolytic solution, which is not preferable because it adversely affects the roughening treatment). ) But representative compounds include the following.
1. Molybdenum: Sodium molybdate (dihydrate)
2. Iron: Ferrous sulfate (7 water salt)
3. Cobalt: Cobalt sulfate (7 hydrate)
4). Nickel: Nickel sulfate (7 water salt)
[0019]
As the acidic copper electrolytic bath, any acid can be used as long as it is a mineral acid, but usually a sulfuric acid bath (containing copper sulfate as copper) is used.
[0020]
The liquid composition and temperature of the copper sulfate-sulfuric acid bath can be selected in a wide range, but the limit current density of the bath shows the respective values by them, so the current density to be used depends on the liquid composition and liquid temperature, Depending on the movement of the liquid, etc., it is also different depending on whether only `` bake plating '' is applied, or whether normal copper plating, zinc plating, nickel plating, etc. are further applied on the capsule. It is necessary to adjust.
[0021]
Illustrative liquid conditions for an acidic copper electrolytic bath suitable for industrial use are as follows.
1. Copper: 5-50g / l
2. Molybdenum: 0.001 to 5 g / l
3. Other: 0.01 to 10 g / l
4). Acid: 10 to 100 g-H 2 SO 4 / l
5. Liquid temperature: Room temperature to 50 ° C
[0022]
Further, the amount of circulation of the bath is not particularly limited, but it is preferable that the lower limit is the amount of replenishment of the consumed components of the bath, and the upper limit is that the region near the cathode surface does not become a significant turbulent region.
[0023]
In addition, since the processing time is practically and preferably in the range of several seconds to several tens of seconds, it is preferable to set operation conditions such as liquid composition and current density so that a desired group of fine protrusions can be completed in such a time. .
[0024]
In the method for producing a copper foil of the present invention, subsequent to the step of forming the “burnt plating layer”, a “copper plating layer” or “nickel plating layer”, “zinc plating” is formed on the “burnt plating layer”. Layer ”or“ nickel plating layer ”and“ zinc plating layer ”may be performed, and if desired, further on the“ copper plating layer ”after the“ copper plating layer ”formation step. The step of forming “nickel plating layer” or “zinc plating layer” or “nickel plating layer” and “zinc plating layer” may be performed, and further, the “copper plating layer” formation step or the “nickel” Following the “plating layer” forming step, the “zinc plating layer” forming step or the “nickel plating layer” and the “zinc plating layer” forming step, the “copper plating layer” or the “nickel plating layer”, “zinc plating layer” Or Kell plating layer "and step may be carried out to form a chromate film on the" galvanized layer ". The conditions for these additional steps may follow those of known methods.
[0025]
In addition, the copper foil to be processed in the production method of the present invention may be an electrolytic copper foil or a rolled copper foil. This is because the type of the copper foil is not selected in the method of the present invention.
[0026]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in more detail based on examples. However, the present invention is not limited to these.
[0027]
Example 1
(1) Copper foil to be treated (raw copper foil)
Electrolytic copper foil (untreated copper foil; thickness: 18 μm; mat surface roughness: R a = 0.6 μm; R z = 4.2 μm; manufactured by Furukawa Circuit Foil Co., Ltd.)
(2) Formation of burnt plating layer The raw copper foil was subjected to cathodic electrolysis with direct current under the following conditions, and a "bake plating layer" consisting of fine protrusions was electrodeposited on the mat surface of the raw copper foil. .
(1) Electrolyte composition ・ Copper sulfate: 100g-CuSO 4・ 5H 2 O / l
・ Sulfuric acid: 120 g-H 2 SO 4 / l
・ Molybdenum: 0.6g-Na 2 MoO 4・ 2H 2 O / l
Iron: 15g-FeSO 4 · 7H 2 O / l
(2) Electrolyte temperature: 35 ° C
(3) Current density: 40A / dm 2
(4) Processing time: 3.5 sec.
(3) The raw copper foil on which the fine projection group was formed on the capsule plating mat surface was subjected to cathodic electrolysis with direct current under the following conditions, and the fine projection group was covered with a thin copper layer.
(1) Electrolyte composition ・ Copper sulfate: 250g-CuSO 4・ 5H 2 O / l
・ Sulfuric acid: 100 g-H 2 SO 4 / l
(2) Electrolyte temperature: 50 ° C
(3) Current density: 20 A / dm 2
(4) Processing time: 7.0 sec.
(4) Further, the processing of (2) → (3) was repeated once more.
(5) Surface treatment Nickel-phosphorus plating (0.1 mg / dm 2 ) and zinc plating (0.1 mg) on the surface of the obtained copper foil (hereinafter referred to as “roughened copper foil”) to be bonded. / dm 2 ), and further a chromate treatment (hereinafter referred to as “surface-treated copper foil”) was prepared.
[0028]
The characteristics of the obtained surface-treated copper foil were evaluated for the following items, respectively.
[0029]
(1) Peel strength Normal surface peel according to 5.7 of JIS C 6481 “Testing method for copper-clad laminates for printed wiring boards” using the obtained surface-treated copper foil pressed and bonded to an FR-4 substrate as a sample. (Normal “stripping strength”) was measured.
[0030]
(2) Hydrochloric acid degradation rate After pressing and bonding the obtained surface-treated copper foil to the FR-4 base material, the surface-treated copper foil was etched to a width of 1 mm as a sample, and JIS C 6481 “Printed Wiring Board In accordance with 5.7 of “Copper-laminated laminate test method”, normal peel and post-degradation peel (so that the sample is immersed in a treatment solution at 25 ° C. mixed with the same amount of 35% hydrochloric acid and distilled water for 1 hour "Strength", hereinafter referred to as "peel after deterioration") was measured and obtained by calculation according to the following formula.
Hydrochloric acid deterioration rate (%) = (1− (peel after degradation / normal peel)) × 100
[0031]
(3) A test paper (Toyo filter paper No. 2) was placed on the surface-treated copper foil from which powder was removed, and the test paper was dragged in the horizontal direction by 150 mm while a load (250 g / 20 mmφ) was applied thereto. The copper powder adhering to the test paper was visually observed and evaluated in the order of A <B <C <D <E <F according to the amount of adhesion (A: powder falling “zero”, F: most powder falling) ).
[0032]
The results are shown in Table 1.
[0033]
Example 2
A roughened copper foil and a surface-treated copper foil were produced in the same manner as in Example 1 except that the composition of the electrolytic solution in the treatment (2) was changed to the following, and Example 1 of the surface-treated copper foil was prepared. The same characteristic evaluation was performed. The results are shown in Table 1.
<1> Composition of copper sulfate electrolytic solution: 100g-CuSO 4 · 5H 2 O / l
・ Sulfuric acid: 120 g-H 2 SO 4 / l
・ Molybdenum: 0.05g-Na 2 MoO 4・ 2H 2 O / l
・ Tungsten: 0.05g-Na 2 WO 4・ 2H 2 O / l
[0034]
Example 3
A roughened copper foil and a surface-treated copper foil were produced in the same manner as in Example 1 except that the composition of the electrolytic solution in the treatment (2) was changed to the following, and Example 1 of the surface-treated copper foil was prepared. The same characteristic evaluation was performed. The results are shown in Table 1.
<1> Composition of copper sulfate electrolytic solution: 100g-CuSO 4 · 5H 2 O / l
・ Sulfuric acid: 120 g-H 2 SO 4 / l
・ Molybdenum: 0.6g-Na 2 MoO 4・ 2H 2 O / l
Iron: 15g-FeSO 4 · 7H 2 O / l
Tungsten: 0.03 g-Na 2 WO 4 · 2H 2 O / l
[0035]
Example 4
A roughened copper foil and a surface-treated copper foil were produced in the same manner as in Example 1 except that the composition of the electrolytic solution in the treatment (2) was changed to the following, and Example 1 of the surface-treated copper foil was prepared. The same characteristic evaluation was performed. The results are shown in Table 1.
(1) Electrolyte composition ・ Copper sulfate: 100g-CuSO 4・ 5H 2 O / l
・ Sulfuric acid: 120 g-H 2 SO 4 / l
・ Molybdenum: 0.6g-Na 2 MoO 4・ 2H 2 O / l
Cobalt: 10g-CoSO 4 · 7H 2 O / l
[0036]
Example 5
A roughened copper foil and a surface-treated copper foil were produced in the same manner as in Example 1 except that the composition of the electrolytic solution in the treatment (2) was changed to the following, and Example 1 of the surface-treated copper foil was prepared. The same characteristic evaluation was performed. The results are shown in Table 1.
(1) Electrolyte composition ・ Copper sulfate: 100g-CuSO 4・ 5H 2 O / l
・ Sulfuric acid: 120 g-H 2 SO 4 / l
・ Molybdenum: 0.6g-Na 2 MoO 4・ 2H 2 O / l
Nickel: 10g-NiSO 4 · 7H 2 O / l
[0037]
Comparative Example 1
A roughened copper foil and a surface-treated copper foil were produced in the same manner as in Example 1 except that the composition of the electrolytic solution in the treatment (2) was changed to the following, and Example 1 of the surface-treated copper foil was prepared. The same characteristic evaluation was performed. The results are shown in Table 1.
(1) Electrolyte composition ・ Copper sulfate: 100g-CuSO 4・ 5H 2 O / l
・ Sulfuric acid: 120 g-H 2 SO 4 / l
・ Arsenic: 0.4cc / l as 60% H 3 AsO 4 (Specific gravity: 1.58)
[0038]
Comparative Example 2
A roughened copper foil and a surface-treated copper foil were produced in the same manner as in Example 1 except that the composition of the electrolytic solution in the treatment (2) was changed to the following, and Example 1 of the surface-treated copper foil was prepared. The same characteristic evaluation was performed. The results are shown in Table 1.
(1) Electrolyte composition ・ Copper sulfate: 100g-CuSO 4・ 5H 2 O / l
・ Sulfuric acid: 120 g-H 2 SO 4 / l
・ Molybdenum: 0.6g-Na 2 MoO 4・ 2H 2 O / l
[0039]
The roughened copper foils obtained in Examples 1, 4, 5, Example 2, 3 and Comparative Examples 1 and 2 were subjected to roughening treatment on a sulfuric acid-hydrogen peroxide soft etching solution (H 2 SO 4 : 100 g / l, H 2 O 2 : 30 g / l, n-propanol: 10 cc / l) for 1 minute to dissolve the roughened film, and evaporate the solution to dryness to dissolve the solution. After decomposing and removing hydrogen peroxide contained in the solution, quantitative analysis of the target element in the solution is performed by atomic absorption spectrometry (using a Hitachi Z Corp. Z-6100 polarized Zeeman atomic absorption spectrophotometer). went. The results are shown in Table 2. In addition, data are converted into the abundance in the roughened film.
[0040]
[Table 1]
Figure 0003739929
[0041]
[Table 2]
Figure 0003739929
[0042]
【The invention's effect】
As shown in Table 1, the copper foil of the present invention has performance that is comparable to that using arsenic (a conventional technique) that has strong peel strength, resistance to hydrochloric acid deterioration, and powder fall off co-toxicity. On the other hand, it can be seen that the copper foil for a single molybdenum cited as another example of the prior art (not including a poison) has a low peel strength, a large amount of powder fall off, and a large practical problem.
That is, according to the present invention, it is possible to provide an environment-friendly copper foil that sufficiently satisfies the predetermined performance as a copper foil for printed wiring boards and a manufacturing method therefor.

Claims (9)

原銅箔の被接着面側表面に、やけめっき金属元素が、モリブデンと、鉄、コバルト、ニッケルの内の少なくとも1種と、からなる銅のやけめっき層を有することを特徴とするプリント配線板用銅箔。  A printed wiring board having a copper burnt plating layer composed of molybdenum and at least one of iron, cobalt and nickel on the surface to be bonded of the raw copper foil. Copper foil. 前記のやけめっき層の上に銅のめっき層を更に有する請求項1に記載のプリント配線板用銅箔。  The copper foil for printed wiring boards according to claim 1, further comprising a copper plating layer on the burnt plating layer. 前記の銅のやけめっき層又は銅のめっき層の上に、ニッケルめっき層又は亜鉛めっき層若しくはニッケルめっき層と亜鉛めっき層を更に有する請求項1又は2に記載のプリント配線板用銅箔。  The copper foil for printed wiring boards according to claim 1, further comprising a nickel plating layer, a zinc plating layer, a nickel plating layer, and a zinc plating layer on the copper burnt plating layer or the copper plating layer. 前記の銅のめっき層又はニッケルめっき層、亜鉛めっき層若しくはニッケルめっき層と亜鉛めっき層の上に、クロメート皮膜を更に有する請求項2又は3に記載のプリント配線板用銅箔。  The copper foil for printed wiring boards according to claim 2 or 3, further comprising a chromate film on the copper plating layer, the nickel plating layer, the zinc plating layer, or the nickel plating layer and the zinc plating layer. 酸性銅電解浴を用い、被処理銅箔を陰極とし、該浴の限界電流密度付近の電流密度で電解して該銅箔表面に銅のやけめっき層を形成するプリント配線板用銅箔の製造方法において、該浴の電解液中に、溶液の形態での、銅のやけめっき層のやけめっき金属元素が、モリブデンの0.001〜5g/lと、鉄、コバルト、ニッケルの少なくとも1種の0.01〜10g/lと、からなることを特徴とする方法。  Manufacture of copper foil for printed wiring boards using an acidic copper electrolytic bath, with the copper foil to be treated as a cathode, and electrolyzing at a current density near the limiting current density of the bath to form a copper burnt plating layer on the surface of the copper foil In the method, in the electrolyte solution of the bath, the burnt plating metal element of the copper burnt plating layer in the form of a solution is 0.001 to 5 g / l of molybdenum and at least one of iron, cobalt, and nickel. A method characterized by comprising 0.01 to 10 g / l. 前記のやけめっき層を形成する工程に次いで、該やけめっき層の上に銅のめっき層を形成する工程を行う請求項5に記載のプリント配線板用銅箔の製造方法。  The manufacturing method of the copper foil for printed wiring boards of Claim 5 which performs the process of forming a copper plating layer on this burn plating layer following the process of forming the said burn plating layer. 前記のやけめっき層を形成する工程又は銅のめっき層を形成する工程に次いで、該銅のやけめっき層又は該銅のめっき層の上に、ニッケルめっき層又は亜鉛めっき層若しくはニッケルめっき層と亜鉛めっき層を形成する工程を行う請求項5又は6に記載のプリント配線板用銅箔の製造方法。  Next to the step of forming the burnt plating layer or the step of forming the copper plating layer, a nickel plating layer or a zinc plating layer or a nickel plating layer and zinc on the copper burnt plating layer or the copper plating layer. The manufacturing method of the copper foil for printed wiring boards of Claim 5 or 6 which performs the process of forming a plating layer. 前記の銅のめっき層又はニッケルめっき層、亜鉛めっき層若しくはニッケルめっき層と亜鉛めっき層を形成する工程に次いで、該銅のめっき層又はニッケルめっき層、亜鉛めっき層若しくはニッケルめっき層と亜鉛めっき層の上に、クロメート皮膜を形成する工程を行う請求項6又は7に記載のプリント配線板用銅箔の製造方法。  Following the step of forming the copper plating layer or nickel plating layer, zinc plating layer or nickel plating layer and zinc plating layer, the copper plating layer or nickel plating layer, zinc plating layer or nickel plating layer and zinc plating layer The manufacturing method of the copper foil for printed wiring boards of Claim 6 or 7 which performs the process of forming a chromate membrane | film | coat on top. 前記の電解浴が硫酸銅−硫酸浴である請求項5乃至8のいずれか1に記載のプリント配線板用銅箔の製造方法。  The method for producing a copper foil for a printed wiring board according to any one of claims 5 to 8, wherein the electrolytic bath is a copper sulfate-sulfuric acid bath.
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