Method for producing titanium foil or titanium sheet, and cathode electrode
11359298 · 2022-06-14
Assignee
Inventors
- Tetsuya Uda (Kyoto, JP)
- Kouhei Funatsu (Kyoto, JP)
- Akihiro KISHIMOTO (Kyoto, JP)
- Kenichi Mori (Tokyo, JP)
- Hideki Fujii (Tokyo, JP)
Cpc classification
C25D1/20
CHEMISTRY; METALLURGY
C25D3/54
CHEMISTRY; METALLURGY
International classification
C25D1/20
CHEMISTRY; METALLURGY
C25D3/54
CHEMISTRY; METALLURGY
Abstract
A titanium foil or a titanium sheet is produced by electrodeposition from molten salt using constant current pulse, the method comprising: forming an electrodeposited titanium film on a surface of a cathode electrode made of glassy carbon, graphite, Mo, and Ni, and separating thereafter the electrodeposited titanium film from the cathode electrode by performing one or both of applying an external force to the electrodeposited titanium film and removing the cathode electrode. This enables the electrodeposited titanium film electrodeposited on the cathode electrode to be peeled from the cathode electrode simply and at low cost.
Claims
1. A method for producing a titanium foil or a titanium sheet by electrodeposition from molten salt using constant current pulse, the method comprising: forming an electrodeposited titanium film on a surface of a cathode electrode made of one or more kinds selected from glassy carbon, graphite, Mo, and Ni, and thereafter separating the electrodeposited titanium film from the cathode electrode, wherein the separating process comprises steps of: on an interface between the electrodeposited titanium film and the cathode electrode, forming a grasping portion in the electrodeposited titanium film by removing a portion of the cathode electrode, and thereafter, a) peeling the electrodeposited titanium film from the cathode electrode with the grasping portion as a starting point, or b) bonding a separation member to the grasping portion and then peeling the electrodeposited titanium film from the cathode electrode with the separation member as the starting point.
2. The method for producing a titanium foil or a titanium sheet according to claim 1, wherein the process of removing comprises a step of: removing by physical means or chemical means.
Description
BRIEF DESCRIPTION OF DRAWINGS
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DESCRIPTION OF EMBODIMENTS
(20) The present invention will be described. The following describes a case of a production of a titanium foil, as an example; however, the present invention enables a production of a titanium sheet having a sheet thickness of about 100 μm to 1 mm by making an electrolytic apparatus large in scale or by performing the electrodeposition for a long time. A thickness of a titanium foil or a titanium sheet obtained by the present invention is 30 μm to 1 mm.
(1) Electrodeposition from Molten Salt Using Constant Current Pulse
(21) In the present invention, electrodeposition from molten salt using constant current pulse is employed to form an electrodeposited titanium film on a surface of a cathode electrode that is made of one or more kinds selected from glassy carbon, graphite, Mo, and Ni. Note that, in experiments described in the present specification, a strip-like electrode about 10 mm wide and 50 mm long is used as the cathode electrode. In an industrial-scale production, an electrode having a width of about 300 to 1000 mm and a length of about 500 to 2500 mm is supposed to be used. In particular, an electrode of any size commensurate to a titanium sheet to be produced is available in the present invention. To one end of the electrode, a conducting wire is connected. The electrolysis is performed with the other end of the electrode immersed in molten salt by about 10 mm. The electrode includes a fixing portion (e.g., through hole) used to, for example, screw down the electrode to fix it at a given location.
(22) In the present invention, molten salt electrolysis using constant current pulse is employed. As a molten salt electrolytic bath, it is preferable to prepare one obtained by adding titanium ion, which serves as a titanium source in reduction and precipitation, to an alkali metal chloride bath or a mixture bath of an alkali metal chloride and an alkaline earth metal chloride. Some kinds of the chlorides may be replaced with an iodide. By feeding current between an anode electrode and the cathode electrode, titanium is caused to precipitate on a surface of the cathode electrode.
(23) The electrolytic bath prepared in the present invention contains no fluorine. Of alkali metal chlorides, it is preferable to use LiCl, NaCl, KCl, or CsCl. Of alkaline earth metal chlorides, it is preferable to use MgCl.sub.2 or CaCl.sub.2.
(24) In the present invention, unlike the Kroll process or the like, use of the electrodeposition from molten salt makes it possible to obtain a titanium foil directly from titanium compound material without producing sponge titanium. This can reduce the burden of processes of melting, casting, blooming, and in addition, repeating rolling and annealing, which can suppress an increase in stages, complexity, and production costs.
(25) In addition, the molten salt bath contains no highly poisonous fluorides, which facilitates industrial operation.
(26) Furthermore, as compared with fluorides, the alkali metal chlorides are inexpensive; in particular, NaCl and KCL are less expensive than LiCl, and the present invention therefore has an advantage also in this regard. Moreover, when a plurality of kinds of the alkali metal chlorides and the alkaline earth metal chlorides are mixed at close to their eutectic composition, the mixture has a lower fusing point, which is preferable.
(27) For example, when nearly equimolar amounts of NaCl and KCl are mixed, the mixture has a low fusing point. A preferable range is NaCl-30 to 70 mol % KCl, and a more preferable range is NaCl-40 to 60 mol % KCl.
(28) In a case of MgCl.sub.2—NaCl—KCl molten salt, when they are mixed at Mg:Na:K=50:30:20 (mol %) in cation ratio, the molten salt has a low fusing point. A preferable range is Mg:Na:K=40 to 60:20 to 40:10 to 30.
(29) It is preferable that the raw material of titanium mainly includes titanium chlorides. TiCl.sub.4 has a low degree of solubility in the molten salt, and it is therefore particularly preferable to melt TiCl.sub.2 to contain divalent titanium ion. In addition, TiCl.sub.2 requires less number of electrons in its reduction than multivalent titanium ions such as a tetravalent titanium ion, and therefore TiCl.sub.2 produces more precipitation amount of titanium with the same quantity of electricity than the multivalent titanium ions, which is preferable.
(30) The divalent titanium ion can be obtained also by mixing TiCl.sub.4 (tetravalent) and metallic titanium (zerovalent). TiCl.sub.4 is used also in a current process of titanium smelting, and impurities in TiCl.sub.4 can be reduced by distillation, which is advantageous to management of concentration of the impurities. In addition to the titanium chlorides, metallic titanium such as titanium scraps and sponge titanium can be used as the titanium source. The divalent titanium ion can be obtained by partial reduction of TiCl.sub.4 (tetravalent) with Na, Mg, or Ca.
(2) Cathode Electrode
(31) Forming the cathode electrode used in the electrodeposition from molten salt using constant current pulse from one or more kinds selected from glassy carbon, graphite, Mo, and Ni makes it possible to separate an electrodeposited titanium film caused to precipitate on the cathode electrode easily and at low cost using physical external force or the like.
(32) The reason for this is unclear; however, it is presumed that such materials resist being alloyed with the electrodeposited titanium.
(33) In the present invention, the “glassy carbon” refers to non-graphitizing carbon, which combines glass and ceramic properties, and is referred to also as “glassy carbon.” The glassy carbon is used as conductive materials, crucible, parts of a prosthesis, and the like and has properties including high-temperature resistance, high hardness, low density, low electric resistance, low friction, low thermal resistance, high chemical resistance, impermeability to gases and liquids, and the like.
(34) In Examples, a glassy carbon plate from Tokai Fine Carbon Co., Ltd, which was mirror finished and 2.0 mm thick, was used as a glassy carbon-made electrode as remaining non-surface-treated.
(35) In Examples, a graphite plate from Tokai Fine Carbon Co., Ltd, which was 5.0 mm thick, was used as a graphite-made electrode as remaining non-surface-treated.
(36) A Mo-made electrode refers to an electrode made of molybdenum having a purity of 99% or higher. In Examples, a molybdenum plate from Japan Metal Service, Co., Ltd, which was 99.95% pure and 0.1 mm thick, was used as the Mo-made electrode as remaining non-surface-treated.
(37) A Ni-made electrode refers to an electrode made of nickel having a purity of 99% or higher. In Examples, a nickel plate from Japan Metal Service, Co., Ltd, which was 99+% pure and 0.2 mm thick, was used as the Ni-made electrode as remaining non-surface-treated.
(38) The glassy carbon-made or graphite-made electrode allows an electrodeposited titanium film formed on a surface of the electrode to be separated easily by applying external force without using a jig, chemical agent, or the like.
(39) The Mo-made electrode allows an electrodeposited titanium film to be separated by, for example, using a jig such as tweezers, pincers, and pliers, or a chemical agent such as one containing, for example, nitric acid: sulfuric acid: water=1:1:3. The Ni-made electrode allows an electrodeposited titanium film to be separated by, for example, using a jig such as tweezers, pincers, and pliers, or a chemical agent such as concentrated hydrochloric acid and dilute nitric acid. On the Ni-made electrode, the electrodeposited titanium film can be separated without using these jig and chemical agent, depending on the situation, although the separation has a problem in its repeatability.
(40) A glassy carbon-made or Mo-made cathode electrode leaves an extremely small amount of its electrode substance adhered to a surface of a separated titanium foil (electrodeposited titanium film), which lightens a load of removing the electrode substance. In addition, the separated titanium foil (electrodeposited titanium film) has an excellent metallic luster on its surface, providing a high quality in the appearance.
(41) Note that the cathode electrode may be entirely made of one or more kinds selected from glassy carbon, graphite, Mo, and Ni, and alternatively, a body of the electrode may be made of another material as long as at least the surface of the electrode for electrodepositing titanium is made of one or more kinds selected from these materials. As the body of the electrode, for example, a starting material having a sufficient conductivity and strength required of the electrode, such as stainless steel plate, non-stainless steel plate, and copper, can be used. This can reduce a consumption of glassy carbon, graphite, Mo, or Ni, enabling cost reduction. The number of kinds of these electrode materials to be used is not limited to one, and a plurality of kinds of these electrode materials can be used in combination.
(3) Summary of Electrolysis Conditions
(42) In the electrolysis, constant current pulse for on/off control is used as applied current. The pulse current for on/off control means that the current is fed in such a manner as to alternate feeding a current for reduction and precipitation to the cathode electrode for a certain period of time to cause titanium to be reduced to precipitate on the cathode electrode, and thereafter cutting off the current for a certain period of time, with a value of the current left unchanged.
(43) If the current for reduction and precipitation is continuously fed, titanium ions existing in a vicinity of the surface of the cathode electrode decrease through the reduction and precipitation. At this point, titanium ions conveyed from off the cathode electrode are not necessarily supplied to the vicinity of the electrode evenly at a constant rate commensurate with the decrease in the titanium ions existing in the vicinity of the electrode. This can make a concentration of titanium ions existing in the vicinity of the cathode electrode uneven, which is considered to be a cause of inhibiting the titanium precipitate from being smoothed.
(44) In contrast, by providing a current cut-off time in the electrolysis, concentration diffusion occurs during this cut-off time, eliminating or mitigating the unevenness of titanium ions. Use of the pulse current is therefore considered to have an effect of averaging the concentration of titanium ions on a periphery of an interface of the precipitation, which enables the smoothing.
(45) A pulse width of the applied current preferably has a pulse frequency of 0.1 to 10 Hz, more preferably 0.25 to 2 Hz. That is, it is preferable to set an energization period t.sub.on, during which the current is continuously fed, at 0.05 to 5 s and set a non-energization period t.sub.off, during which the current is cut off, at 0.05 to 5 s, similarly, and more preferable to set energization period t.sub.on=non-energization period t.sub.off=0.25 to 2 s.
(46) A value of cathode current may be any value as long as the cathode current has a constant current amount (cathode current density) above a certain amount that allows the electrodeposition of titanium.
(4) An Example of Electrolysis Conditions
(47) Investigations about electrodeposition conditions for obtaining a smooth electrodeposited titanium film (particularly about a pulse period) conducted by the present inventors, experiments conducted by the present inventors to determine the pulse period, and analysis results of the experiments will be described below.
(48) First, non-energization periods t.sub.off with which a smooth electrodeposited titanium film was obtained and non-energization periods t.sub.off with which a smooth electrodeposited titanium film was not obtained were investigated for various energization periods t.sub.on; next based on the investigations as a precondition, potentials during current application and potentials after current cut-off were measured, to estimate optimal energization period t.sub.on and non-energization period t.sub.off. Thereafter, the precondition was examined by performing the electrodeposition from molten salt actually under the electrolysis conditions.
(4-1) Experimental Method
(49) The electrodeposition of titanium was performed by the following method.
(50) Molten salt: MgCl.sub.2—NaCl—KCl eutectic salt (Mg:Na:K=50:30:20/mol %) (5 mol % TiCl.sub.2 (cation ratio))
(51) Working electrode: Mo or glassy carbon, Counter electrode: Ti, Reference electrode: Ti
(52) Current density: −0.200 or −0.400 A/cm.sup.2
(53) In the investigations of the conditions for obtaining a smooth electrodeposited titanium film, a Mo-made substrate was used, with current density set at −0.200 A/cm.sup.2 and energization amount set at 181.8 C/cm.sup.2 (equivalent to a titanium film having a thickness: 100 μm). After the electrolysis, the substrate used as the working electrode was subjected to leaching treatment to extract adhered salts in 5 mass % hydrochloric acid.
(54) In addition, from a difference in mass of a sample before and after the electrolysis, a current efficiency was determined. In a current cut-off method, the measurements were performed using a Mo-made substrate and a glassy carbon-made substrate, with current density set at −0.200 A/cm.sup.2 or −0.400 A/cm.sup.2 and energization period t.sub.on changed as 0.5 s.fwdarw.1.0 s.fwdarw.1.5 s.fwdarw.2.0 s.fwdarw.2.5 s.fwdarw.3.0 s.fwdarw.3.5 s.fwdarw.4.0 s.fwdarw.4.5 s.fwdarw.5.0 s.fwdarw.10.0 s.
(4-2) Experimental Results and Review
(55)
(56)
(57) Based on the graph illustrated in
(58)
(59) TABLE-US-00001 TABLE 1 t.sub.on t.sub.off t.sub.off/t.sub.on 1.5 0.40 0.267 2.0 0.55 0.275 2.5 0.75 0.300 3.0 0.95 0.317 3.5 1.15 0.329 4.0 1.30 0.325 4.5 1.50 0.333 5.0 1.70 0.340
(60) As illustrated in the graph of
(61) Here, in order to examine whether the assumption that the time taken by the potential to exceed the threshold value of −0.043 V after the current cut-off was set as the non-energization period t.sub.off was correct, the electrolysis was performed with a Mo-made substrate used, current density=−0.200 A/cm.sup.2, energization period t.sub.on=5.0 s, and non-energization period t.sub.off=1.7 s.
(62)
(63) Next, in order to examine whether a smooth electrodeposited titanium film can be obtained with the energization period t.sub.on=5.0 s, the electrolysis was performed using a Mo-made substrate, with current density=−0.200 A/cm.sup.2, energization period t.sub.on=5.0 s, and non-energization period t.sub.off=5.0 s. At this point, the energizing amount was set at 545.0 C/cm.sup.2 (equivalent to an electrodeposited titanium film having a thickness: 300 μm).
(64)
(65) From the above results, it is necessary to make a new assumption to determine the non-energization period t.sub.off from the potentials before and after the current cut-off.
(66)
(67) Although no investigations about the conditions for obtaining a smooth electrodeposited titanium film was conducted for the cases of
(68)
(69) From the graphs of
(70) From the above review, in a case of using the Mo-made substrate, the following (i) and (ii) are preferably satisfied, and in a case of using the glassy carbon-made substrate, the following (iii) is preferably satisfied.
(71) (i) The period t.sub.on is set at not more than 5 s when the current density is −0.200 mA/cm.sup.2.
(72) (ii) The period t.sub.on is set at not more than 1.5 s when the current density is −0.400 mA/cm.sup.2.
(73) (iii) The period t.sub.on is set at not more than 5 s when the current density is −0.200 mA/cm.sup.2.
(74) By employing the electrolysis conditions described above, a smooth electrodeposited titanium film can be manufactured. Here, “being smooth” means that the electrodeposited substance has few pores, is dense, and has a surface with small unevenness. In addition, “not being smooth” means that protrusion-like or dendrite-like electrodeposited substances are scattered on the surface of the electrode, and there are many pores when the surface or a cross section of the electrode is observed.
(5) Separation of Electrodeposited Titanium Film From a Cathode Electrode
(75) After the electrodeposited titanium film is formed in such a manner, a titanium foil is produced by separating the electrodeposited titanium film from the cathode electrode by performing one or both of a process of applying an external force to the electrodeposited titanium film and a process of removing at least a portion of the cathode electrode.
(76) In the present invention, it is preferable to separate the electrodeposited titanium film from the electrode by grasping directly a portion of the electrodeposited titanium film and peeling the electrodeposited titanium film from the electrode or bonding a separation member to a portion of the electrodeposited titanium film, grasping the separation member, and peeling the electrodeposited titanium film from the electrode. The portion of the electrodeposited titanium film refers to a region serving as a possible starting point of peeling, such as a corner or an edge of the electrodeposited titanium film.
(77) In a case where the cathode electrode will not be reused, a possible example is one in which at least the portion of the cathode electrode is removed by physical means such as grinding, cutting, polishing, ion milling, and blasting or chemical means such as etching, by which the electrodeposited titanium film is separated.
(78) In the present invention, only one of the process of applying the external force to the electrodeposited titanium film and the process of removing at least the portion of the cathode electrode may be performed, but both of them are preferably performed. For example, the electrodeposited titanium film may be separated from the cathode electrode by, on an interface between the electrodeposited titanium film and the cathode electrode, removing a portion of the cathode electrode (e.g., a portion including a region serving as a possible starting point of the peeling, such as a corner and an edge of the electrodeposited titanium film of the electrodeposited titanium film) to form a grasping portion in the portion of the electrodeposited titanium film, and thereafter, peeling the electrodeposited titanium film from the cathode electrode with the grasping portion as the starting point or by bonding a separation member to the grasping portion and then peeling the electrodeposited titanium film from the cathode electrode with the separation member as the starting point.
(79) Examples of a metal adhesive used to bond the separation member to the electrodeposited titanium film include “Metal Lock Y611 Black S” (trade name),” an acrylic adhesive from Cemedine co., ltd.
(80) The removal of the cathode electrode is preferably performed by, for example, physical means such as grinding, cutting, polishing, ion milling, and blasting or chemical means such as etching.
(81) According to the present invention, a titanium foil or a titanium sheet having a film thickness of about 100 μm to 1 mm can be produced without concurrent use of a physical action such as applying vibrations to a cathode electrode or agitating a molten salt bath, by causing a smooth electrodeposited titanium film to precipitate on a cathode electrode simply and separating the smooth electrodeposited titanium film from the cathode electrode reliably and quickly.
(82) The titanium foil obtained by the present invention may be further reworked as necessary. This can further enhance a dimensional accuracy and mechanical properties of the titanium foil.
(83) According to the present invention, a smooth titanium foil can be produced without performing a process of melting, casting, blooming, and in addition, repeating rolling and annealing, and without an increase in cost of peeling an electrodeposited titanium film from a cathode electrode, which thus enables a significant reduction in production costs through reduction in processes and improvement in yield.
(84) A thickness of a titanium foil or a titanium sheet produced by the present invention is about 100 μm to 1 mm. According to “JIS H4600:2012 Titanium and titanium alloys-Sheets, plates and strips”, a plate has a thickness of not less than 0.2 mm.
EXAMPLE 1
(85) Investigations were conducted on possibilities of separation of electrodeposited titanium films electrodeposited on various kinds of substrates, and analyses of the electrodeposited titanium films were conducted.
(1) Experimental Method
(86) The electrodeposition of titanium was performed by the following method.
(87) Molten salt: MgCl.sub.2—NaCl—KCl eutectic salt (Mg:Na:K=50:30:20/mol %) (5 mol % TiCl.sub.2 (cation ratio))
(88) Working electrode: Mo, stainless steel (SUS304), Fe, Ti, Nb, Ta, Ni, Counter electrode: Ti, Reference electrode: Ti
(89) Current density: −0.232 A/cm.sup.2
(90) Energizing amount: 908.3 C/cm.sup.2 (equivalent to an electrodeposited titanium film having a thickness: 500 μm)
(91) Pulse width: Energization period t.sub.on=Non-energization period t.sub.off=0.5 s
(92) After the electrolysis, the substrate used as the working electrode was subjected to leaching treatment to extract adhered salts in 5 mass % hydrochloric acid. Thereafter, the substrate and the electrodeposited titanium film were cut at a portion in a vicinity of their boundary, and from this portion, the electrodeposited titanium film was separated.
(93) For electrodeposited titanium films electrodeposited on the Mo-made substrate and the SUS304-made substrate, a portion of each substrate was etched using an acid (sulfuric acid:nitric acid:water=1:1:3 for Mo, and 10 mass % HCl for SUS304) to form a holding portion used for applying external force to the electrodeposited titanium film to separate the electrodeposited titanium film from the substrate, grasping the holding portion of the electrodeposited titanium film and peeling the electrodeposited titanium film from the substrate, by which a titanium foil having a thickness equivalent to 500 μm that is calculated from energizing amount was obtained.
(94) A substrate-side surface of the electrodeposited titanium film separated from the substrate was subjected to SEM observation and WDS analysis (wavelength-dispersive X-ray spectroscopic analysis) using an EPMA. In addition, from a difference in mass of a sample before and after the electrolysis, a current efficiency was determined.
(2) Experimental Results and Review
(95) Table 2 gives current efficiencies and succeed/failure in the separation of the substrates.
(96) TABLE-US-00002 TABLE 2 Current efficiency Success/Failure Substrate (%) in separation Mo-made #01 62.60 x (∘ after etching) Mo-made #02 55.22 x SUS-made #01 82.96 x (Δ after etching) SUS-made #02 35.60 x Fe-made #01 82.21 x Ti-made #01 56.73 x Nb-made #01 75.70 x Ta-made #01 65.61 x Ni-made #01 70.48 x Ni-made #02 70.17 ∘
(97) Of the various kinds of substrates subjected to this test, substrates with which electrodeposited titanium films were successfully separated by the above method, including “after etching”, include Mo-made #01 substrate and Ni-made #02 substrate. With SUS-made #01 substrate, a part of an electrodeposited titanium film can be separated after the etching, but the electrodeposited titanium film was torn during its separation.
(98)
(99)
(100) In addition,
(101) As illustrated in
(102) Table 3 gives results of quantitative analysis (at %) conducted on pointed spots 1 and 2 on
(103) TABLE-US-00003 TABLE 3 Ti O Mo 1 93.50 6.48 0.02 2 93.49 6.48 0.03
(104) TABLE-US-00004 TABLE 4 Ti O Ni 1 63.78 26.15 10.07 2 83.68 13.18 3.14 3 85.99 12.18 1.83
(105) TABLE-US-00005 TABLE 5 Ti O C Fe Ni Cr 1 88.93 8.89 2.08 0.06 0.01 0.03 2 36.82 46.12 2.79 7.99 2.81 3.47 3 43.39 38.03 3.42 8.92 2.97 3.26
(106) As given in Table 3, very little Mo is present on Mo-made #01 substrate. In contrast, as given in Tables 4 and 5, it can be seen that Ni-made #02 substrate and SUS-made #01 substrate include many portions that contain metallic elements originating from Ni-made #02 substrate and SUS-made #01 substrate.
EXAMPLE 2
(107) By using cross sections of electrodeposited titanium films electrodeposited on a glassy carbon-made substrate and a graphite-made substrate, and the substrates, how carbon diffused in and adhered on electrodeposited titanium films was investigated by conducting observation and analysis on substrate sides of the electrodeposited titanium films.
(1) Experimental Method
(108) The electrodeposition of titanium was performed by the following method.
(109) Molten salt: MgCl.sub.2—NaCl—KCl eutectic salt (Mg:Na:K=50:30:20/mol %) (5 mol % TiCl.sub.2 (cation ratio))
(110) Working electrode: glassy carbon (glassy carbon-made #01, 02) and graphite (graphite-made #01, 02), Counter electrode: Ti, Reference electrode: Ti
(111) Current density: −0.232 A/cm.sup.2
(112) Energizing amount: 900.5 C/cm.sup.2 (equivalent to an electrodeposited titanium film having a thickness: 500 μm)
(113) After the electrolysis, the substrate used as the working electrode was subjected to leaching treatment to extract adhered salts in 5 mass % hydrochloric acid. X-ray diffraction analysis was thereafter conducted on Glassy carbon-made #01 and Graphite-made #01 from which titanium films were peeled. Glassy carbon-made #02 and Graphite-made #02 were cut after embedded in resin.
(114) Substrate-side surfaces of the peeled electrodeposited titanium films and cross sections of the substrates embedded in resin were subjected to SEM observation and WDS analysis (wavelength-dispersive X-ray spectroscopic analysis) using an EPMA. In addition, from a difference in mass of a sample before and after the electrolysis, a current efficiency was determined.
(2) Experimental Results and Review
(115) Table 6 gives experimental conditions and current efficiency of each substrate.
(116) TABLE-US-00006 TABLE 6 Current Energizing Current density amount efficiency Substrate (A/cm.sup.2) (C/cm.sup.2) (%) Glassy carbon-made −0.232 900.5 80.3 #01 Glassy carbon-made 82.4 #02 Graphite-made 80.5 #01 Graphite-made 91.7 #02
(117) As given in Table 6, the current efficiencies fell within the range from 80% to about 90%.
(118)
(119) As illustrated in
(120)
(121) As illustrated in
(122)
(123) As illustrated in the graph of
EXAMPLE 3
(124) By the same experimental method as Example 2, electrodeposited titanium films were formed on cathode electrodes (substrates) made of Mo, SUS, Ti, Nb, Ta, Ni, glassy carbon, and graphite, and whether the electrodeposited titanium films could be peeled by hand or by means other than by hand, and in addition, whether impurities originating from the substrates were present on the peeled surface of the substrates were checked.
(125) Results of the checks are illustrated in
(126) TABLE-US-00007 TABLE 7 Impurities on peeled surface Peeled by Peeled by originating hand other means from substrate Mo #03 x Metal adhesive Δ Absent (torn during separation) Mo #01 x Etching ∘ Absent SUS #01 x Etching Δ Present (torn during (Fe, Cr, Ni) separation) Ti #01 x Metal adhesive x — Nb #01 x Metal adhesive x — Ta #01 x Metal adhesive x — Ni #01 x Metal adhesive x — Ni #02 ∘ — Present (Ni) Glassy carbon-made ∘ — A little (C) #01-1 Glassy carbon -made ∘ — Absent #01-2 Graphite-made ∘ — Present #02 (C)
(127)
(128) As illustrated in
(129) Additionally, contamination on the peeled surface from the glassy carbon-made, graphite-made, Ni-made, and Mo-made substrates, was practically at insignificant levels.