Method of making electrodeposited copper foil

Abstract: Disclosed is a method of making electrodeposited copper foil which comprises carrying electrolysis by adding a water-soluble cellulose ether to an electrolytic solution. A profile of the matte side nodules of the electrodeposited copper foil obtained by the method of the present invention can be easily controlled, and the electrodeposited copper foil which is high above IPC specification Class 3 in elongation at room temperature and high temperature can be obtained.

Description: This invention relates to method of making electrodeposited copper foil, more particularly to method of making electrodeposited copper foil suitable for a printed circuit. Electrodeposited copper foil for a printed circuit has been commercially manufactured by contacting an electrolytic solution of copper sulfate aqueous solution with an insoluble anode such as lead and a cathode rotary drum made of stainless steel or titanium, to get electrodeposited copper on the cathode drum, which is then wound continuously. Generally, when an aqueous solution contains only copper ion and sulfuric acid ion in electrolytic solution, pivoting or microporosity is generated on the copper foil due to dust or oil involuntarily existing in the system. This causes serious problems for practical use. Also, the shape of promontories on a matte side which contacts with the electrolytic solution deforms so that sufficient adhesion strength cannot be obtained when adhering the foil to an insulating material at later stage. Further, it leads to the problem that roughness becomes so large that insulation resistance between conductor layers or circuit conductivity becomes low, or transfer of copper to unwanted area and undercut of the conductor after etching are increased whereby various properties of the printed circuit are damaged. In order to prevent pinholing, a chloride ion may be added in the electrolytic solution, or the electrolytic solution filtered by passing it through a filter containing an activated carbon to remove dust and oils. Also, for preventing microporosity and improving the shape of the matte side promontories, glue has heretofore been added to the electrolytic solution and it has been proposed to add various organic, inorganic materials as additives other than glue. However, a material which is industrially more excellent than glue has never been discovered from the point of quality stabilities of a copper foil obtained therefrom. In recent years, developments in electronic circuit technology including development of semiconductors and integrated circuits are remarkable, and in the printed circuit board, boards such as single-sided and double-sided boards to multilayer boards having tens of layers have been generated for general-purpose because of improvement in each technology such as insulation, laminating, drilling, interlayer connection, etching, component mounting, heat dissipation and printed board inspection systems. As the technology movement, since high density wiring has increasingly demanded, the abilities of highly multilayered, fine pattern and large-sized board are becoming remarkable. For a number of high multilayers, the insulating layers and conductors should be made thin. For fine patterning, it is required to make a conductor thin, prevent foil crack and decrease undercut at etching. Also, for a large-sizied multilayer board, dimensional stability is necessary. Thus, for the copper foil itself as the conductive foil, improved insulating and dielectric characteristics, decreased conductor resistance and low profile (decrease in roughness) of the matte side to reduce undercut as well as improved high temperature elongation to prevent foil crack due to thermal stress have become required. Low profiling of the matte side can be accomplished, for example, by adding a large amount of glue as mentioned above to the electrolytic solution. However, accompanying the increase of the amount of glue added, room temperature and high temperature elongation characteristics are abruptly lowered. On the other hand, a copper foil obtained from an electrolytic solution containing no glue which is passed through an activated carbon filter has extremely high elongation at room temperature and high temperature, but the shape of the promontories deforms and roughness increases. Further, when electrodeposition current density is suppressed to low levels, the resulting foil has low profile and is improved in elongation as compared with a foil prepared with high current density. However, it is hard to make the low profile uniform to the desired degree and productivity becomes low, whereby it is not preferred from an economical view. US 3784454 describes brightener compositions for aqueous copper pyrophosphate electroplating electrolyte consisting essentially of (1) a heterocyclyic brightening additive selected from the group consisting of mercaptothiazoles, mercaptobenzthiazoles, mercaptothiadiazoles, mercaptopyrimidines, and mercaptoiminazoles, and (2) and auxiliary brightener selected from the group of step plating inhibitors consisting of imino diacetic acid, malonic acid, cinammic acid, aurine tricarboxylic acid, aliphatic dicarboxylic acids having at least seven carbon atoms, salts of the aforesaid acids and hydroxyethyl cellulose, said auxiliary brightener being in a proportion of from 3:1 to 3:4 based on the weight of said heterocyclic brightener. The present invention aims to provide a method of making electrodeposited copper foil having high elongation at high temperature and a low profile matte side, which can meet the demand from high density wiring of a printed circuit board with ease and economy. The present invention provides an electrolytic method of making electrodeposited copper foil comprising adding from 0.1 to 10 ppm (based on the electrolytic solution) of a water-soluble cellulose ether, wherein said cellulose ether is a compound in which a part or all of three hydroxyl groups of a unit cellulose represented by the following formula: is/are etherified with a substituent (s) to an electrolytic solution consisting essentially of an acid aqueous copper sulfate solution. Fig. 1 is a graph showing a test result of Example 2. Preferred water-soluble cellulose ether may preferably include those in which a substituent for etherification has, for example, a hydroxyl group at the terminal or those having an ionic substituent in which a terminal hydrogen of a carboxyl group is replaced by a monovalent cation, and further preferably a water-soluble cellulose ether combinedly having ether linkages on a plurality of different substituents. As exemplary compounds which are industrially and cheaply produced, there may be mentioned, for example, sodium carboxymethyl cellulose, potassium carboxymethyl cellulose, ammonium carboxymethyl cellulose, hydroxyethyl cellulose, sodium carboxymethylhydroxyethyl cellulose, potassium carboxymethylhydroxyethyl cellulose and ammonium carboxymethylhydroxyethyl cellulose. Other than the above, water-soluble ethers of methyl cellulose and cyanoethyl cellulose may be also used. Solubility of the cellulose ether varies depending on the degree of etherification of cellulose ether, i.e. degree of substitution (D.S., an average number of hydroxyl groups of cellulose which are substituted and etherified by substituents, the maximum value for D.S. is 3), or molar substitution (M.S., an average molar number of substituents added to each cellulose unit, theoretical maximum value for M.S. is infinity), but it may be any one so long as water-soluble. Those which are industrially produced generally have a D.S. value of 0.5 to 1.5 and a M.S. value of 1 to 2 or so. The reason why the cellulose ether is limited to water-soluble ones is that the electrolytic solution is an aqueous solution so that it must mix uniformly in the electrolytic solution. Powder state ones may be thrown into a tank and dissolved at dissolving a copper starting material. However, when a filter such as activated carbon is used, at least a part of the cellulose ether dissolved is adsorbed and removed so that the cellulose ether is preferably dissolved in water or hot water previously to prepare an aqueous solution and then mixed in an electrolytic solution with a pump immediately before supplying a solution in an electrodeposited tank. Generally, according to the added amount of the cellulose ether, matt height can be suppressed and roughness becomes small, providing substantially no effect to the elongation value. However, if it is less than 0.1 ppm, its effect is too small, while it is added in excess of 10 ppm, roughness cannot be improved any more and economically undesired. The cellulose ether may be used in combination with other additives. For example, it may be added with glue, and high elongation can be obtained as compared with glue alone while elongation is slightly lowered due to addition of glue. Accordingly, the effect of adding cellulose ether itself is clear in this case. When the cellulose ether is added to an electrolytic solution as described above, a copper foil electrodeposited at a cathode has fine nodules as compared with that to which cellulose ether is not added. Also, excessive growth of nodules to the direction of thickness of the foil which is a characteristic of a usual electrodeposited copper foil can be prevented and concentration of current can be inhibited whereby uniform growth can be promoted to X-Y direction. Thus, as compared with the conventional electrodeposited copper foil, recrystallization at lower temperature can easily be performed, and elongation at room temperature and high temperature and folding endurance can be improved. While detailed mechanism is unclear, according to addition of the cellulose ether, decrease in electrolytic polarization voltage is great by lowering in oxygen overvoltage at an anode and lowering in copper ion concentration overvoltage at a cathode interface. And thus, copper electrodeposition reaction can be performed rapidly and uniformly, whereby growth of crystals and crystal boundary to the direction of thickness can be suppressed. EXAMPLES In the following, examples of the present invention will be explained. Example 1 To the above copper sulfate aqueous solution which had been passed through an activated carbon filter were added each 1 % aqueous solution of glue, sodium carboxymethyl cellulose or hydroxyethyl cellulose with amounts as shown below based on the flow amount of the copper sulfate aqueous solution supplyed to an electrodeposited tank. By using the thus prepared electrolytic solution, and lead for an anode and a rotary drum made of titanium for a cathode, electrolysis was carried out with a current density of 50 A/dm² to prepare a copper foil having a thickness of 35 µm and compared with each other. Five points average of the matte side roughness R max , tensile strength with elongation-trans at room temperature and maintained at 180 °C for 5 minutes, elongation and folding endurance by using MIT fold tester of the resulting copper foil were measured with n = 2, respectively. Also, inspection of presence or absence of pinhole·microporosity was effected by the dye penetration method. The results are shown in Table 1. Example 2 In the same manner as in Sample No. 1, 3 and 6 of Example 1 except for electrolyzing the current density of 100 A/dm², copper foils were prepared having a thickness of 18 µm, 35 µm and 70 µm, respectively. Regarding these copper foils, the matte side roughness R max was measured. The results are shown in Fig. 1. As described above, according to the present invention, profile of the matte side of the electrodeposited copper foil can be easily controlled, and the electrodeposited copper foil which is high above IPC specification Class 3 in elongation at room temperature and high temperature can be obtained. Thus, it can be applied to a copper foil for an internal and external layer of a high density wiring multilayer board and also to a copper foil for a flexible base material since folding endurance has been improved. Further, the method of the present invention is to simply add an additive to an electrolytic solution which has conventionally been used so that it is easy and the already installed facilities can be utilized whereby industrial and economical effects are also remarkable.

Claims: An electrolytic method of making electrodeposited copper foil comprising adding from 0.1 to 10 ppm (based on the electrolytic solution) of a water-soluble cellulose ether, wherein said cellulose ether is a compound in which a part or all of three hydroxyl groups of a unit cellulose represented by the following formula: is/are etherified with a substituent (s), to an electrolytic solution consisting essentially of an acidic aqueous copper sulfate solution. A method as claimed in Claim 1, wherein said water-soluble cellulose ether is selected from the group consisting of sodium carboxymethyl cellulose, potassium carboxymethyl cellulose, ammonium carboxymethyl cellulose, hydroxyethyl cellulose, sodium carboxymethylhydroxyethyl cellulose, potassium carboxymethylhydroxyethyl cellulose, ammonium carboxymethylhydroxyethyl cellulose, methyl cellulose and cyanoethyl cellulose.

Inventors: AKUTSU TSUKASA C O FURUKAWA CR, FUKUDA RYOSAKU C O FURUKAWA CR, KAMIYAMA OSAMU C O FURUKAWA CR, MATSUKI NOBORU C O FURUKAWA CR, NAKATSUGAWA HIROSHI C O FURUKA, TANI TOSHIO C O FURUKAWA CRT F, AKUTSU, TSUKASA, FUKUDA, RYOSAKU, KAMIYAMA, OSAMU, MATSUKI, NOBORU, NAKATSUGAWA, HIROSHI, TANI, TOSHIO, AKUTSU, TSUKASA, C/O FURUKAWA CRT. FOIL CO. LTD., FUKUDA, RYOSAKU, C/O FURUKAWA CRT. FOIL CO. LTD., KAMIYAMA, OSAMU, C/O FURUKAWA CRT. FOIL CO. LTD., MATSUKI, NOBORU, C/O FURUKAWA CRT. FOIL CO. LTD., NAKATSUGAWA, HIROSHI, C/O FURUKAWA CRT FOIL CO LTD, TANI, TOSHIO, C/O FURUKAWA CRT. FOIL CO. LTD.
Applicants: FURUKAWA CIRCUIT FOIL, FURUKAWA CIRCUIT FOIL CO., LTD.
Application year: 1990
Main classification: C25D1
IPC codes: C25D1