TECHNICAL FIELD
[0001] The present invention relates to a method for anodizing an aluminum alloy and to
a power supply for anodizing an aluminum alloy.
BACKGROUND OF THE INVENTION
[0002] Conventionally, anodizing of an aluminum alloy is carried out in a bath containing
an aqueous solution of sulfuric acid, oxalic acid, phosphoric acid or the like to
form an oxide film or coating on a surface of the aluminum alloy for the purpose of
increasing the hardness, wear resistance and corrosion resistance of the surface or
coloring the surface. An anodic oxide film has a dense barrier layer and a porous
layer both composed of Al
2O
3.
[0003] As methods of applying electric power to obtain a film with desired properties, a
direct current anodizing method, a periodic reverse electrolyzing method, a method
using superimposed direct current on an alternating current, a pulse anodizing method
and so on have been reported (
Kinzoku Hyomen Gijutsu (Metal Surface Technology) 39, p.512 (1988),
Journal of Aluminum Finishing Society of Kinki, No.1334, p.1 (1988), Japanese Unexamined Patent Application Publication No.
2000-282294, Japanese Unexamined Patent Application Publication No.
2004-35930).
[0004] When a high voltage is applied to supply a large current in order to achieve a high
film formation rate in a direct current anodizing method, a large amount of Joule
heat is generated in the barrier layer to cause a defect called "burning of anodic
oxide coating" on the oxide film. Thus, it is difficult to form a thick anodic oxide
film on a molded aluminum product and an aluminum die-cast product, containing a large
amount of Si, Cu or Fe and having poor electrical conductivity, within a short period
of time by a direct current anodizing method.
[0005] It is said that a pulse electrolysis method including the periodic reverse electrolyzing
method is better than a direct current anodizing method to form a desired oxide film
free of a defect called "burning of anodic oxide coating" within a short period of
time with high productivity. For example, it is reported in
Kinzoku Hyomen Gijutsu, 39, p.512 (1988) that an oxide film can be formed at a high rate by a periodic reverse electrolyzing
method in which a negative current is intermittently supplied to a sulfuric acid bath
at an oxidation voltage lower than that used in a direct current anodizing method.
It is reported in
Journal of Aluminum Finishing Society of Kinki, No.1334, p.1 (1988) that when aluminum A1080P (JIS H4100) was subjected to electrolysis by a periodic
reverse electrolyzing method in a bath containing 20 wt % sulfuric acid and 10 g/L
oxalic acid at 20°C for 65 minutes under the conditions involving a frequency of 13.3
Hz, a current density of 4 A/dm
2 and a duty of 95 %, an aluminum anodic oxide film with a thickness of 92 µm (1.4
µm/min) was obtained. In these methods, however, since a voltage having a frequency
in the order of 10 Hz is applied, the film formation rate cannot be increased in the
case of an aluminum die-cast product containing a large amount of alloy elements.
In addition, since a positive voltage and a negative voltage must be applied, a power
supply having a complicated bipolar structure is required.
[0006] Japanese Unexamined Patent Application Publication No.
2000-282294 discloses that an aluminum anodic oxide film with a high heat resistance and a corrosion
resistance can be formed on an aluminum alloy surface by a method using superimposed
direct current on an alternating current under such an electrolysis condition that
the AC component does not contain a negative component and the AC component is at
least 5 % of the level of the DC component. However, the current density suitably
employed is as low as 0.1 to 2 A/dm
2. With such a current density, the film formation rate is so low as to cause problems
of low productivity and high cost. In addition, the power supply system required for
this method is also complicated since both an AC power supply and a DC power supply
are required.
[0007] Japanese Unexamined Patent Application Publication No.
2004-35930 suggests, as a technique which can increase the formation rate of an aluminum anodic
oxide film for the purpose of improving productivity, a method in which a sine wave
current with a high frequency of 200 to 5000 Hz (preferably 600 to 2000 Hz) on which
a DC current is superimposed is supplied to a sulfuric acid aqueous solution bath.
That is, a high-frequency sine wave with a frequency of 1000 Hz and a voltage of ±
20 V on which a DC voltage of 19.8 V was superimposed was supplied to aluminum alloy
ADC12 (JIS H5302) in a 10% sulfuric acid aqueous solution at 17°C for an electrolytic
treatment period of 20 minutes, thereby obtaining an anodic oxidation film with a
thickness of 22 µm (growth rate: 1.1 µm/min). It is reported that the current density
obtained five minutes after the start of electrolysis was 13.8 A/dm
2. However, the method is still disadvantageous in that the frequency is limited to
200 to 5000 Hz and in that, since a sine wave is used, the amount of current which
can be supplied per unit time is smaller as compared to a rectangular wave. In addition,
the power supply system required for this method is also complicated since both an
AC power supply and a DC power supply are required.
[0008] Japanese Unexamined Patent Application Publication No.
2006-83467 discloses a method for forming an anodic oxide film having cells which have grown
in random directions relative to a surface of aluminum or aluminum alloy and thus
have no orientation for the purpose of improving the corrosion resistance and impact
resistance. In one specific method using an alloy containing impurities such as silicon,
a step of applying a plus voltage and a step of removing electric charge are repeated.
The plus voltage is applied for 25 to 100 µs (5 to 20 KHz in terms of frequency) at
a time. During the step of removing electric charge, the application of the plus voltage
is stopped and a short circuit is formed between the anode and cathode or a minus
voltage is applied across the anode and the cathod. It is shown that when a minus
voltage is applied, such a minus voltage is applied for the same time period as that
for which the plus voltage is applied. The reason why electric charge is removed is
as follows. Namely, when an electric charge is accumulated, the resistance substantially
increases so that a high voltage must be applied in order to obtain a constant current
value. As a result, the before-mentioned defect called "burning of anodic oxide coating"
occurs.
[0009] In this method, however, since the film formed is reduced by electrolysis when a
minus voltage is applied, the film growth rate cannot be improved. Also, it has been
found that a negative current with a large negative current density flows, when a
short circuit is formed between the anode and the cathode. For example, when the positive
current density was 18A/dm
2 under an anodizing condition, the negative current density was 12.8 A/dm
2. Thus, there still remains a room for improvement to increase the film growth rate.
SUMMARY OF THE INVENTION
[0010] The present invention has been made in view of the above problems, and it is, therefore,
an object of the present invention to provide a method for anodizing an aluminum alloy
and a power supply for anodizing an aluminum alloy capable of increasing the film
formation rate and improving productivity without developing a defect called "burning
of anodic oxide coating" by suppressing or preventing a negative current when anodizing
of an aluminum alloy is carried out by a pulse electrolysis method.
Another object of the present invention is to provide a method for anodizing an aluminum
alloy and a power supply for anodizing an aluminum alloy capable of further increasing
the film formation rate to improve productivity by setting a frequency of pulse voltage
that allows a maximum current to flow when the pulse voltage is applied.
[0011] For the purpose of accomplishing the above objects, the present invention provides
the following inventions.
[1]A method for anodizing an aluminum alloy to form an anodic oxide film on a surface
of said aluminum alloy using pulsed electric power, characterized in that, after application
of a positive pulse voltage, a short circuit is formed between an anode for anodic
oxidation and a cathode for anodic oxidation for a short-circuit duration of not longer
than15 µs during non application of the pulse voltage.
[2] A method for anodizing an aluminum alloy as recited in [1] above, wherein said
short-circuit duration is not shorter than 1 µs and not longer than 15 µs.
[3] A method for anodizing an aluminum alloy as recited in [1] above, wherein said
short-circuit duration is not shorter than 1 µs and not longer than 5 µs.
[4] A method for anodizing an aluminum alloy as recited in [1], [2] or [3] above,
wherein said pulsed electric power has a waveform having a cycle composed, in the
order, of a pulse voltage application duration (T+), a dead time (Td) and a short-circuit duration (Ts).
[5] A method for anodizing an aluminum alloy as recited in [1], [2] or [3] above,
wherein said pulsed electric power has a frequency of 8 to 35 KHz.
[6] A method for anodizing an aluminum alloy as recited in [1], [2] or [3] above,
wherein said pulsed electric power has a frequency of 10 to 30 KHz.
[7] A method for anodizing an aluminum alloy as recited in [4] above, wherein said
pulsed electric power has a frequency of 8 to 35 KHz.
[8] A method for anodizing an aluminum alloy as recited in [4] above, wherein said
pulsed electric power has a frequency of 10 to 30 KHz.
[9] A power supply for anodizing an aluminum alloy for use in a method for anodizing
an aluminum alloy to form an anodic oxide film on a surface of said aluminum alloy
using pulsed electric power, comprising a pulsed electric power generating section
configured to generate such pulsed electric power that, after application of a positive
pulse voltage, a short circuit is formed between a terminal connected to an anode
for anodic oxidation and a terminal connected to a cathode for anodic oxidation for
a short-circuit duration of not longer than 15 µs during non application of the pulse
voltage.
[10] A power supply for anodizing an aluminum alloy as recited in [9] above, wherein
said pulsed electric power generating section is configured to generate pulsed electric
power which provides a short-circuit duration of not shorter than 1 µs and not longer
than 15 µs.
[11] A power supply for anodizing an aluminum alloy as recited in [9] above, wherein
said pulsed electric power generating section is configured to generate pulsed electric
power in which the short-circuit duration is not shorter than 1 µs and not longer
than 5 µs.
[12] A power supply for anodizing an aluminum alloy as recited in [9], [10] or
[11] above, wherein said pulsed electric power generating section is configured to
generate pulsed electric power having a waveform composed, in the order, of a pulse
voltage application duration (T+), a dead time (Td) and a short-circuit duration (Ts).
[13] A power supply for anodizing an aluminum alloy as recited in [9], [10] or [11]
above, wherein said pulsed electric power generating section is configured to generate
pulsed electric power having a frequency of 8 to 35 KHz.
[14] A power supply for anodizing an aluminum alloy as recited in [9], [10] or [11]
above, wherein said pulsed electric power generating section is configured to generate
pulsed electric power having a frequency of 10 to 30 KHz.
[15] A power supply for anodizing an aluminum alloy as recited in [12] above, wherein
said pulsed electric power generating section is configured to generate pulsed electric
power having a frequency of 8 to 35 KHz.
[16] A power supply for anodizing an aluminum alloy as recited in [12] above, wherein
said pulsed electric power generating section is configured to generate pulsed electric
power having a frequency of 10 to 30 KHz.
[0012] In a method according to the present invention for forming an anodic oxide film on
a surface of an aluminum alloy using pulsed electric power, a short-circuit is formed,
after application of a positive pulse voltage, between the anode for anodic oxidation
and the cathode for anodic oxidation for a very short short-circuit duration during
non application of the pulse voltage so that a negative current is controlled to be
reduced or eliminated. As a consequence, there can be provided a method for anodizing
an aluminum alloy and a power supply for anodizing an aluminum alloy that are capable
of increasing the film formation rate and of improving productivity without developing
a defect known as "burning of anodic oxide coating". According also to the present
invention, there can be provided a method for anodizing an aluminum alloy and a power
supply for anodizing an aluminum alloy that are capable of giving an effect that the
film formation rate can increase and the productivity can be improved by setting the
frequency of the pulse voltage to a value permitting a maximum current to flow when
the pulse voltage is applied in addition to the above effect attained by the formation
of a short-circuit between the anode for anodic oxidation and the cathode for anodic
oxidation.
BRIEF DESCRIPTION OF DRAWINGS
[0013]
FIG. 1 is a graph showing the relationship between the film growth rate and the effective
current density in an aluminum alloy anodizing method using pulsed electric power,
wherein the effective current density refers to a difference between the positive
current density that is achieved when a pulse voltage is applied and the negative
current density that flows during non application of the pulse (effective current
density = positive current density - negative current density).
FIG. 2 is a view illustrating a structure of a power supply and an electrolytic bath
for carrying out the aluminum alloy anodizing method of the present invention.
FIG. 3 is an explanatory view of a pulse setting condition and actual voltage and
current waveforms corresponding to the pulse setting condition.
FIG. 4 is an explanatory view of a steady state of film growth during anodizing.
FIG. 5 is an explanatory view of the relationship between the current waveform and
frequency of pulsed electric power used in the present invention.
FIG. 6 is a table showing the experiment results in Examples and Comparative Examples
of the present invention.
FIG. 7 illustrates the relationship between the short-circuit duration and the negative
current in the present invention.
DETAILED DESCRIPTION OF THE INVENTION
[0014] Description will be hereinafter made of the present invention in detail.
The present inventors have made a study for the purpose of increasing the film formation
rate and found that when a short circuit is formed, after one application of a positive
pulse voltage, between an anode for anodic oxidation and a cathode for anodic oxidation
to cause a negative current (current which flows in a direction opposite the direction
in which a current flows when the pulse is applied) to flow during non application
of the pulse voltage, it is possible to reduce the concentration gradients of Al
3+ and O
2- ions in the barrier layer formed during application of the pulse voltage and to discharge
the electric double layer at the solid-liquid interface so that a large current can
be allowed to flow in the next application of the pulse voltage. However, as described
before, the problem is that the magnitude of negative current is large relative to
the magnitude of the positive current which flows when a pulse voltage is applied.
The present inventors have thus conducted a further study on this issue.
[0015] The present inventors have found that the film growth rate is proportional to the
effective current density (FIG. 1), when a short circuit is formed between the anode
for anodic oxidation and the cathode for anodic oxidation during non application of
a pulse voltage in a method for anodizing an aluminum alloy using pulsed electric
power. It has also been found, however, that a problem is caused because when the
effective current density is increased, the negative current also increases.
[0016] The present inventors have investigated a method capable of further improving the
film growth rate in order to improve productivity. As a result, the present inventors
unexpectedly found that when a short circuit is formed, after one application of a
positive pulse voltage, between the anode for anodic oxidation and the cathode for
anodic oxidation for a very short period of time during non application of the pulse
voltage, the negative current can be reduced or even prevented so that a large current
can be allowed to flow without developing a defect known as "burning of anodic oxide
coating" when the next positive pulse voltage is applied. The present inventors also
found that the film growth rate can be significantly increased when the frequency
of the pulse voltage to be applied is set to a value within a specified range. The
present invention has been made based on the above findings.
[0017] A method for anodizing an aluminum alloy according to the present invention is characterized
in that pulsed electric power is used and that a short circuit is formed, after application
of a positive pulse voltage, between the anode for anodic oxidation and the cathode
for anodic oxidation for a short-circuit duration of not longer than 15 µs during
non application of the pulse voltage. The short-circuit duration is preferably not
shorter than 1 µs and not longer than 15 µs, more preferably not shorter than 1 µs
and not longer than 5 µs, still more preferably not shorter than 1 µs and not longer
than 3 µs. While the preferred range of the short-circuit duration depends on the
type or electrical conductivity of the aluminum alloy to be treated, the negative
current can be significantly reduced or even prevented from flowing and a large current
can be allowed to flow in the next application of positive pulse voltage when the
short-circuit duration is within the above range. Therefore, the film formed is not
reduced by a negative current and the film growth rate can be significantly increased
without developing a defect known as "burning of anodic oxide coating." It has been
considered necessary to remove all the electric charges accumulated in the system
by forming a short circuit or applying a negative voltage before the next application
of a positive pulse voltage in order both to prevent a defect called "burning of anodic
oxide coating" and to increase the film growth rate. However, as a result of a zealous
study, the present inventors have found that when only the electric charges at the
barrier layer interfaces (Al/Al
2O
3 interface and Al
2O
3/electrolytic solution interface) at which the oxide film is being formed are removed,
a substantially reduced electrical resistance state can be realized so that a large
current necessary to form a good film is allowed to flow when the next positive pulse
voltage is applied. With this method, the film growth rate can be significantly increased
since the film formed can be prevented from being melted and reduced by a large negative
current.
[0018] In the present invention, it is preferred that the pulsed electric power have a waveform
having a cycle composed, in the order, of a pulse voltage application duration (T
+), a dead time (T
d), and a short-circuit duration (T
s). In this case, to improve the film formation rate, the pulse voltage application
duration (T
+) is preferably approximately 20 to 100 µs, and the dead time (T
d) is preferably approximately 5 to 10 µs.
[0019] It is also preferred that the pulsed electric power have a frequency of 8 to 35 KHz,
more preferably 10 to 30 KHz. When the frequency is within the above range, a quantity
of electricity that can further increase the film growth rate can be supplied to form
a film, which, in conjunction with the effect of the short circuit for a very short
period of time, further increases the film growth rate.
[0020] FIG. 2 is a view explanatory of the structure of a power supply and an electrolytic
bath for use in anodizing an aluminum alloy according to the present invention. A
power supply P is constituted of a sequencer 10, a positive side DC power supply 11,
a repetition frequency generator 12, a positive side pulse generating circuit 13,
a short-circuit side pulse generating circuit 14, a positive side chopper gate amplifier
(GA) 25, a short-circuit side chopper gate amplifier (GA) 26, a positive side chopper
switch 15, a reverse current prevention diode (D
1) 16, and a short-circuit current control circuit 17, and has output terminals 18
connected respectively to an anode 20 and a cathode 21 in an electrolytic bath 19.
Also provided are a positive side output voltmeter (E
1) 22, an electrolytic bath voltmeter (E
B) 23 and an electrolytic bath ammeter (A
B) 24. Designated as 27 is an electrolytic solution.
[0021] The sequencer 10 controls the repetition frequency generator 12, the positive side
pulse generating circuit 13, the short-circuit side pulse generating circuit 14 and
the positive side DC power supply 11 to transform the waveform of pulsed electric
power for use in the present invention into a prescribed shape. The positive side
DC power supply 11 generates DC power necessary to apply a positive pulse voltage
or positive current pulse set by the sequencer 10. The repetition frequency generator
12 generates a reference repetition frequency necessary for the generation of the
pulsed electric power and supplies it to the positive side pulse generating circuit
13 and the short-circuit side pulse generating circuit 14. The positive side pulse
generating circuit 13 generates a pulse of duration T
+, and the short-circuit side pulse generating circuit 14 generates a pulse of duration
T
s. A dead time (T
d) is preliminarily set in sequencer 10. The positive side chopper gate amplifier (GA)
25 assumes a role of amplifying the pulse signal from the pulse generating circuit
13 to such a level that the positive side chopper switch 15 can operate reliably according
to a pulse width signal determined by the positive side pulse generating circuit 13.
The short-circuit side chopper gate amplifier 26 assumes a role of amplifying the
pulse signal from the short-circuit side pulse generating circuit 14 to such a level
that the short-circuit current control circuit 17 can operate reliably according to
a pulse width signal determined by the short-circuit side pulse generating circuit
14. The positive side chopper switch 15 assumes a role of supplying the electric power
from the positive side DC power supply 11 to the electrolytic bath in a pulsed manner
according to a pulse width signal determined by the positive side pulse generating
circuit 13. The reverse current prevention diode 16 prevents reverse power from flowing
to the side of the positive side DC power supply 11. The short-circuit current control
circuit 17 forms, after application of a positive pulse voltage, a short circuit between
the output terminals 18 of the anode 20 and the cathode 21 for a short-circuit duration
T
s during non application of the pulse voltage.
[0022] Anodizing was conducted using the power supply shown in FIG. 2 under the following
conditions. As a representative example of materials with high electrical conductivity,
a test piece of A1100P was used. The test piece had a size of 50 mm × 50 mm × 1.5
mm (0.53 dm
2). As a representative example of materials with low electrical conductivity, a test
piece of ADC12 was used. The test piece had a size of 50 mm × 50 mm × 3.0 mm (0.56
dm
2). The electrolytic bath contained approximately 200 L of an electrolytic solution,
which was stirred by a liquid circulation and micro-aeration system and cooled by
a plate type heat exchanger. A lead cathode bar and a carbon cathode plate were used.
The bath liquid was free sulfuric acid solution with a concentration of approximately
150 g/L, and the bath liquid temperature was 10°C. The anodizing current density was
variously changed up to 20 A/dm
2. After the anodizing, the test pieces were rinsed with flowing water for approximately
two minutes and forcibly dried using hot air.
[0023] FIG. 3 shows a pulse setting condition and actual voltage and current waveforms corresponding
to the pulse setting condition. In the drawing, T
+ represents the pulse voltage application duration, T
d represents the dead time necessary to decrease the pulse voltage to zero and to form
a short circuit between the electrodes (during which the circuit is open), and T
s represents the short-circuit duration.
The voltage waveform rises according to the setting for T
+, drops very slightly during T
d, and remains at zero during T
s. The current waveform rises sharply to a local maximum and then drops in an early
stage of T
+. The current waveform remains at zero during T
d. Although a large negative current flows instantaneously at the moment when T
s starts, the current waveform then returns to zero quickly and almost no current flows
during T
t. After the elapse of T
t, the negative current increases to a local maximum and then starts decreasing.
[0024] The above waveforms can be explained as follows. According to a non-patent document
(
Formation and Dissolution Behavior of Aluminum Anode Oxide Film, NAGAYAMA seiich,
TAKAHASHI Hideaki and KODA Mitsuru; Kinzoku Hyomen Gijutsu (Metal Surface Technology)
Vol.30, No.9, pp.438 to 456 (1979)), the steady state of anodic oxidation is expressed as shown in FIG. 4 (wherein
FIG. 4(a) is an enlarged view of the barrier layer part in the overall structure of
an anodic oxide film shown in FIG. 4(c)). That is, an anode aluminum alloy and a cathode
carbon are placed in an electrolytic solution. Al is oxidized to Al
2O
3 at the anode, and H
+ ions are reduced to H
2 at the cathode. The growth of the barrier layer is described in the document as follows:
(1) The metal Al in contact with the bottom of the barrier layer is converted into
Al3+ ions by anodic oxidation (FIG. 4(a), (1)):
Al → Al3+ + 3e- (Formula 1)
(2) A part of Al3+ ions generated diffuse in the barrier layer and move into the electrolytic solution
(FIG. 4(a), (2)).
(3) At an interface between an upper part of the barrier layer and the electrolytic
solution, the constituent substance Al2O3 of the barrier layer is dissociated into Al3+ and O2- by the action of a strong electric field (FIG. 4(a), (3)):
Al2O3 → 2Al3+ + 3O2- (Formula 2)
(4) The Al3+ ions generated as above move into the electrolytic solution (FIG. 4(a), (4)), and
(5) The O2- ions generated as above move in the barrier layer (FIG. 4(a), (5)).
(6) The O2, ions having moved through the barrier layer and reached the barrier layer (Al2O3)/Al interface are reacted with metal Al at the boundary to form Al2O3 (FIG. 4(a), (6)):
2Al + 3O2- → Al2O3 + 6e- (Formula 3)
(7) At an interface between an upper part of the barrier layer (Al2O3) and the electrolytic solution, H2O is dissociated into H+ ions and O2- ions by the action of a strong electric field (FIG. 4(a), (7)):
H2O → 2H+ + O2- (Formula 4)
A part of the O
2- ions generated are considered to participate in the generation of Al
2O
3 through the above processes (5) and (6).
The above is the process of growth of the barrier layer, and the anodic oxide film
continues growing through the process.
Here, it is mentioned that the transport numbers of Al
3+ and O
2- are approximately 40 % and approximately 60 %, respectively, when the electric charges
move in the barrier layer in the form of Al
3+ and O
2-. It is also mentioned that the transport number of Al
3+ decreases, that is, the film growth rate increases, as the temperature is lower and
as the oxidation current density is higher.
[0025] Here, the potential gradient in the vicinity of the barrier layer is considered as
shown in FIG. 4(b).
- (1) The Al3+ concentration in the barrier layer is higher on the barrier layer/Al interface side
and lower on the barrier layer/electrolytic solution interface side (FIG. 4(b), (A)).
- (2) The O2- concentration in the barrier layer is lower on the barrier layer/Al interface side
and higher on the barrier layer/electrolytic solution interface side (FIG. 4(b), (B)).
- (3) Since there is a limit to the diffusion speed of Al3+ in Al2O3, Al3+ ions are accumulated at the Al/Al2O3 interface with the progress of electrolysis. Thus, the Al3+ concentration at the interface further increases (FIG. 4(b), (C)).
- (4) Similarly, there is a limit to the diffusion speed of O2- in Al2O3, O2- ions are accumulated at the Al2O3/electrolytic solution interface with the progress of electrolysis. Thus, the O2- concentration at the interface increases (FIG. 4(b), (D)).
[0026] From the above understanding, the voltage waveform and the current waveform in FIG.
3 can be explained as follows.
- (1) It is considered that the voltage waveform slightly drops during Td (FIG. 3, (1 )) because Al3+ ions at the Al/Al2O3 interface and O2- ions at the Al2O3/electrolytic solution interface diffuse to the Al side and the electrolytic solution
side, respectively.
- (2) The current waveform rises sharply in an early stage of T+ (FIG. 3, (2)) because the reactions of Formulas (1), (2) and (3) proceed quickly
with an increase in voltage.
- (3) The current waveform then reaches a local maximum value (FIG. 3, (3)) and then
drops because the concentration gradient (potential barrier) in the barrier layer
including both the interfaces increases with the progress of electrolysis as shown
in FIG. 4 (b).
- (4) When the current value decreases, the applied voltage and the potential barrier
are soon balanced and the current reaches a constant value (FIG. 3, (4)).
- (5) Because the applied voltage is zero (the circuit is in an open state) during Td, the current is also zero (FIG. 3, (5)).
- (6) A current flows for a very short period of time during Ts (FIG. 3, (6)) because the electrostatic charges in the form of Al3+ (or holes) at the Al/Al2O3 interface and O2- (or electrons) at the Al2O3/electrolytic solution interface are released and discharged all at once at the moment
when a short circuit is formed between the electrodes at the beginning of Ts.
- (7) Then, almost no current flows during Tt (FIG. 3, (7)). After the elapse of Tt, the negative current increases to a local maximum and then starts decreasing (FIG.
3, (8)). The negative current is considered to be derived from reverse reactions of
Formulas (1), (2) and (3). It is also considered that Tt is a time constant necessary for the reverse reactions to start and is determined
by the type of the aluminum alloy or the composition of the electrolytic solution.
[0027] From above, when the short-circuit duration T
s is shorter than T
t, almost no negative current flows. It was experimentally confirmed that when A1100P,
which has high electrical conductivity, is used as the Al alloy, almost no negative
current flows when the short-circuit duration T
s is approximately 2 µs. It was also confirmed that when ADC12, which has low electrical
conductivity, is used as the Al alloy, almost no negative current flows when the short-circuit
duration T
s is approximately 15 µs. Therefore, it is estimated that T
t is approximately 2 µs in the case of A1100P and approximately 15 µs in the case of
ADC12. In the case of A1100P, a very small, if any, negative current, flowed as long
as T
t was 5 µs or less, and no negative current was observed when T
t was 2 µs or less. In the case of ADC12, on the other hand, a large negative current
suddenly flowed when T
t exceeded 15 µs. As described above, a preferred short-circuit duration depends on
the quality of material of the Al alloy.
[0028] From above, when the electric charges at the Al/Al
2O
3 interface and the Al
2O
3/electrolytic solution interface in the potential barrier are removed, a large current
can be allowed to flow when the next pulse voltage is applied.
As described above, when the short-circuit duration is approximately 5 µs or less,
preferably 1 to 5 µs, more preferably 1 to 3 µs, in the case of A1100P, the film growth
rate can be improved since the film generated is not reduced by a negative current.
In the case of ADC12, when the short-circuit duration is 15 µs or less, preferably
1 to 15 µs, more preferably 1 to 10 µs, the film growth rate can be improved.
[0029] As shown in FIG. 1, the film growth rate is proportional to the effective current
density. It was found that a decrease in effective current caused by a negative current
which flows when a short circuit is formed can be reduced and consequently the film
growth rate can be improved significantly by significantly shortening the short-circuit
duration. In addition, according to the present invention, the film growth rate can
be further improved by optimizing the pulse frequency.
[0030] FIG. 5 shows the current waveform shown in FIG. 3 in more detail, in which FIG. 5(a)
shows a case where the frequency is low (T
+ is long), and FIG. 5(b) shows a case where the frequency is high (T
+ is short). In the case of FIG. 5(b), T
s is set to 2 µs so that almost no negative current can flow.
The frequency f of the pulse is calculated as follows:
f
(i) = 1/(T
+(i) + T
d + T
s) (Formula 5)
Here, i refers to an i-th frequency of a plurality of frequencies which are tested
for optimization.
The quantity of electricity Q used for the anodizing is the integral S
(i) of the current waveform in FIG. 5. When the frequency at this time is f
(i), Q is obtained as follows;
Q
(i) = S
(i)·f
(i) (Formula 6)
The larger Q
(i) is, the higher the film growth rate will be. It is possible to consider that the
range of T
+(i) which gives a large Q
(i) is between T
+(m) at which the current value reaches a local maximum and T
+(e) which makes Area (a) = Area (b) in FIG. 5.
[0031] From a current waveform obtained in the experiment,

When T
d and T
s are set to the above preferred values, that is, T
d = 5 µs and T
s = 2 µs in the case of A1100P or T
s = 15 µs in the case of ADC12 as shown in FIG. 5(b), the frequencies corresponding
to them are:

In reality, it was confirmed experimentally that anodizing can be carried out without
any problems in a frequency range of 8 to 35 KHz, preferably 10 to 30 KHz.
[Examples]
[0032] The following Examples will further illustrate the present invention. It should be
understood, however, that the present invention is not intended to be limited to the
Examples.
Example 1 and Comparative Example 1
[0033] Using the power supply shown in FIG. 2, anodizing was carried out under the following
conditions. As a representative example of materials with high electrical conductivity,
a test piece of A1100P was used. The test piece had a size of 50 mm × 50 mm × 1.5
mm (0.53 dm
2). The electrolytic bath contained approximately 200 L of an electrolytic solution,
which was stirred by a liquid circulation and micro-aeration system and cooled by
a plate type heat exchanger. A lead cathode bar and a carbon cathode plate were used.
The bath liquid was a free sulfuric acid solution with a concentration of approximately
150 g/L, and the bath liquid temperature was 10°C. The anodizing current density was
variously changed up to 20 A/dm
2. After the anodizing, the test piece was rinsed with flowing water for approximately
two minutes and forcibly dried using hot air.
The positive current supply duration T
+ was 80 µs, and the dead time (circuit open period) T
d was 5 µs. Although the positive current density I
+ to be achieved upon application of a pulse voltage was changed variously, the positive
current density I
+ was fixed at 20A/dm
2 since anodizing was able to be carried out stably when I
+ = 20A/dm
2. The negative current was measured at short-circuit duration T
s of 2, 3, 4, 5, 10, 20 and 40 µs. The results were summarized in a table of FIG. 6
and in FIG. 7.
Almost no negative current flowed when T
s = 2 µs. When T
s < 5 µs, a very small, if any, negative current flowed. Although the rate of increase
of negative current increased when T
s exceeded 5 µs, the negative current was still in an allowable range when T
s was not longer than approximately 15 µs. When T
s exceeded 20 µs, the negative current significantly increased.
That is, when the short-circuit duration T
s is equal to or less than approximately 15 µs, the negative current can be sufficiently
reduced or suppressed to almost zero so that the film growth rate can be improved..
Example 2 and Comparative Example 2
[0034] An experiment was conducted under the same conditions as those in Example 1 except
that the positive current supply duration T
+ was 40 µs, and that the negative current was measured at short-circuit durations
T
s of 2, 5, 10, 20 and 40 µs. The results were summarized in a table of FIG. 6 and in
FIG. 7.
Although almost no negative current flowed when the short-circuit duration was 2 µs,
the negative current increased rapidly as the short-circuit duration T
s increased to 10, 20 and 40 µs. The negative current was in an allowable range when
T
s was not longer than approximately 10 µs. When T
s exceeded 20 µs, the negative current significantly increased.
Example 3
[0035] An experiment was conducted under the same conditions as those in Example 1 except
that a test piece (size: 50 mm × 50 mm × 3.0 mm (0.56 dm
2)) of ADC12, having lower electrical conductivity, was used and that changes in negative
current were observed with T
+, T
d and I
+ fixed as follows: T
+ = 80 µs, T
d = 5 µs, I
+ = 10 A/dm
2. As a result, almost no negative current flowed when T
s was shorter than 15 µs but a large negative current flowed when T
s was equal to or longer than 15 µs.