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| United States Patent Application |
20120031441
|
| Kind Code
|
A1
|
|
Tomita; Hiroshi
;   et al.
|
February 9, 2012
|
SUBSTRATE CLEANING APPARATUS AND SUBSTRATE CLEANING METHOD
Abstract
A substrate cleaning apparatus, comprises a process tank that holds a
mixture containing a hydrogen peroxide solution and sulfuric acid and is
used for cleaning a substrate immersed in said mixture; circulation
piping that extends between a primary side of said process tank on which
said mixture is injected into said process tank and a secondary side of
said process tank on which said mixture is discharged from said process
tank and has a pump for causing circulation of said mixture; a heater
disposed in said circulation piping configured to heat said mixture to a
predetermined temperature; a chemical injection pipe configured to inject
a hydrogen peroxide solution into said circulation piping at a position
between the primary side of said process tank and a secondary side, which
is a downstream side, of said heater; and a filter disposed in said
circulation piping configured to remove particles in said mixture.
| Inventors: |
Tomita; Hiroshi; (Yokohama-Shi, JP)
; Yamada; Hiroaki; (Yokohama-Shi, JP)
; Miyazaki; Kunihiro; (Oita-Shi, JP)
; Onoda; Hajime; (Kawasaki-Shi, JP)
|
| Assignee: |
Kabushiki Kaisha Toshiba
Tokyo
JP
|
| Serial No.:
|
277251 |
| Series Code:
|
13
|
| Filed:
|
October 20, 2011 |
| Current U.S. Class: |
134/108 |
| Class at Publication: |
134/108 |
| International Class: |
B08B 3/00 20060101 B08B003/00 |
Foreign Application Data
| Date | Code | Application Number |
| Nov 1, 2005 | JP | 2005-318292 |
Claims
1-7. (canceled)
8. A substrate cleaning method, in which a mixture containing a hydrogen
peroxide solution and sulfuric acid is held in a process tank in which a
substrate is cleaned by being immersed in said mixture, and said mixture
is made to circulate in circulation piping that has a pump and extends
between a primary side of said process tank on which said mixture is
injected into said process tank and a secondary side of said process tank
on which said mixture is discharged from said process tank, the method
comprising: heating said mixture to a predetermined temperature by a
heater disposed in said circulation piping; injecting a hydrogen peroxide
solution from a chemical injection pipe into said circulation piping at a
position between the primary side of said process tank and a secondary
side, which is a downstream side, of said heater; and removing particles
in said mixture by a filter disposed in said circulation piping.
9. The substrate cleaning method according to claim 8, wherein said
filter is disposed between the primary side of said process tank and the
secondary side of said heater, and said chemical injection pipe injects
the hydrogen peroxide solution into said circulation piping at a position
between a primary side, which is an upstream side, of said filter and the
secondary side of said heater.
10. The substrate cleaning method according to claim 8, wherein the
temperature of said mixture in said process tank falls within a range of
120 degrees Celsius to 160 degrees Celsius.
11. The substrate cleaning method according to claim 9, wherein the
temperature of said mixture in said process tank falls within a range of
120 degrees Celsius to 160 degrees Celsius.
12. The substrate cleaning method according to claim 8, wherein said
substrate is a semiconductor wafer.
13. The substrate cleaning method according to claim 8, wherein said
chemical injection pipe is connected to said circulation piping at a
primary side of said filter.
14. The substrate cleaning method according to claim 8, wherein said
chemical injection pipe is connected to a primary side of said filter.
Description
CROSS-REFERENCE TO RELATED APPLICATION
[0001] This application is based upon and claims the benefit of priority
from the prior Japanese Patent Application No. 2005-318292, filed on Nov.
1, 2005, the entire contents of which are incorporated herein by
reference.
BACKGROUND OF THE INVENTION
[0002] 1. Field of the Invention
[0003] The present invention relates to a substrate cleaning apparatus and
a substrate cleaning method that clean a substrate, in particular, a
semiconductor wafer.
[0004] 2. Background of the Invention
[0005] Typically, a resist on a semiconductor wafer substrate is removed
(cleaned off) by immersing the semiconductor wafer in a chemical (resist
remover) in a remover tank of a substrate cleaning apparatus.
[0006] In a conventional cleaning technique, for example, an SPM (sulfuric
acid-hydrogen peroxide mixture) resist removing process, a mixture (SPM
cleaning fluid) containing sulfuric acid and hydrogen peroxide in a
certain proportion is first produced. Typically, to improve the resist
removing capability, the SPM cleaning fluid serving as a remover is kept
at a high temperature equal to or higher than 100 degrees Celsius, for
example. Generally, hydrogen peroxide (H.sub.2O.sub.2) thermally
decomposes into water (H.sub.2O) and oxygen (O.sub.2). In addition,
hydrogen peroxide has a boiling point of 150 degrees Celsius and
evaporates when heated to such a high temperature. Hydrogen peroxide
tends to thermally decompose and evaporate at high temperatures in this
way, so that the oxidation capability (resist removing capability) of the
SPM cleaning fluid is lowered on the time passes.
[0007] According to an existing measure against this, before introduction
of a semiconductor wafer or the concentration of the SPM cleaning fluid
is managed, a predetermined amount of
hydrogen peroxide solution is
additionally injected into an inner tank (wafer process tank) or an outer
tank (overflow receiving tank) of a process tank at desired intervals,
thereby maintaining the oxidation capability of the SPM cleaning fluid.
[0008] A method of managing the hydrogen peroxide concentration uses a
concentration monitor. However, since the concentration has to be always
kept constant, the amount of usage of the hydrogen peroxide solution and
sulfuric acid increases substantially.
[0009] According to the method in which the hydrogen peroxide solution is
introduced before introduction of the semiconductor wafer described
above, it takes long before the hydrogen peroxide solution is
sufficiently mixed with the circulating mixture to form a uniform SPM
mixture containing the hydrogen peroxide solution and sulfuric acid.
[0010] In the case where the hydrogen peroxide solution is introduced into
the inner tank as described above, the hydrogen peroxide solution having
a low specific gravity cannot be effectively mixed with sulfuric acid and
overflows into the outer tank, and thus, a desired resist removing
capability cannot be obtained.
[0011] Similarly, in the case where the hydrogen peroxide solution is
introduced into the outer tank, since the hydrogen peroxide solution is
not effectively mixed, the hydrogen peroxide solution having a low
specific gravity is not mixed with the sulfuric acid and remains
separated in the upper part of the outer tank. Thus, it takes a
predetermined time before a uniform mixture of sulfuric acid and the
hydrogen peroxide solution is formed, or it is difficult to feed all the
introduced hydrogen peroxide solution to a circulation piping because
some of the hydrogen peroxide solution is discharged from the overflow
pipe rather than being fed to the circulation piping.
[0012] Furthermore, for example, a conventional substrate cleaning
apparatus using the SPM cleaning fluid has a process tank that holds a
mixture containing a hydrogen peroxide solution and sulfuric acid and is
used for cleaning a substrate immersed in the mixture, circulation piping
that extends between a primary side of the process tank on which the
mixture is injected into the process tank and a secondary side of the
process tank on which the mixture is discharged from the process tank and
has a pump for causing circulation of the mixture, a filter disposed in
the circulation piping for removing particles in the mixture, a chemical
tank for additionally injecting a mixture of a hydrogen peroxide solution
and sulfuric acid into the process tank, and a heater for heating the
mixture in the chemical tank (see Japanese Patent Laid-Open No. 6-342780,
for example).
[0013] However, in the conventional substrate cleaning apparatus, the
mixture is heated by the heater to a temperature higher than a
temperature required in the process tank before the mixture is injected
into the process tank. Thus, the SPM cleaning fluid heated to the high
temperature thermally decomposes and evaporates, so that the hydrogen
peroxide concentration of the SPM cleaning fluid decreases. As a result,
a desired SPM cleaning fluid cannot be obtained in the process tank.
[0014] As described above, the conventional technique described above has
a problem that the SPM cleaning fluid cannot have a required resist
removing capability, and the amount of the hydrogen peroxide solution
additionally injected into the SPM cleaning fluid cannot be optimized.
SUMMARY OF THE INVENTION
[0015] According one aspect of the present invention, there is provided: a
substrate cleaning apparatus, comprising a process tank that holds a
mixture containing a hydrogen peroxide solution and sulfuric acid and is
used for cleaning a substrate immersed in said mixture; circulation
piping that extends between a primary side of said process tank on which
said mixture is injected into said process tank and a secondary side of
said process tank on which said mixture is discharged from said process
tank and has a pump for causing circulation of said mixture; a heater
disposed in said circulation piping configured to heat said mixture to a
predetermined temperature; a chemical injection pipe configured to inject
a hydrogen peroxide solution into said circulation piping at a position
between the primary side of said process tank and a secondary side, which
is a downstream side, of said heater; and a filter disposed in said
circulation piping configured to remove particles in said mixture.
[0016] According other aspect of the present invention, there is provided:
a substrate cleaning method, in which a mixture containing a hydrogen
peroxide solution and sulfuric acid is held in a process tank in which a
substrate is cleaned by being immersed in said mixture, and said mixture
is made to circulate in circulation piping that has a pump and extends
between a primary side of said process tank on which said mixture is
injected into said process tank and a secondary side of said process tank
on which said mixture is discharged from said process tank, the method
comprising heating said mixture to a predetermined temperature by a
heater disposed in said circulation piping; injecting a hydrogen peroxide
solution from a chemical injection pipe into said circulation piping at a
position between the primary side of said process tank and a secondary
side, which is a downstream side, of said heater; and removing particles
in said mixture by a filter disposed in said circulation piping.
BRIEF DESCRIPTION OF THE DRAWINGS
[0017] FIG. 1 is a diagram showing a configuration of essential parts of a
semiconductor cleaning apparatus according to a First Embodiment of the
present invention;
[0018] FIG. 2 shows a relationship between the hydrogen peroxide
concentration of the SPM cleaning fluid and the elapsed time from the
injection of the hydrogen peroxide at various temperatures;
[0019] FIG. 3 shows a relationship between the hydrogen peroxide
concentration of the SPM cleaning fluid in the inner tank and the elapsed
time from the start of injection of the
hydrogen peroxide solution;
[0020] FIG. 4 is a flowchart for illustrating a semiconductor cleaning
method according to a First Embodiment of the present invention;
[0021] FIG. 5 shows a configuration of essential parts of a semiconductor
cleaning apparatus according to the Second Embodiment of the present
invention.
DETAILED DESCRIPTION
[0022] In the following, embodiments applying the present invention will
be described with reference to the drawings. In the following description
of the embodiments, the present invention is applied to an SPM cleaning
fluid, which is a mixture of a hydrogen peroxide solution and sulfuric
acid. However, the present invention can be equally applied to other
mixtures containing a
hydrogen peroxide solution and sulfuric acid, such
as a cleaning fluid containing a hydrogen peroxide solution, sulfuric
acid and ozone gas.
First Embodiment
[0023] FIG. 1 is a diagram showing a configuration of essential parts of a
semiconductor cleaning apparatus (substrate cleaning apparatus) according
to a First Embodiment of the present invention.
[0024] As shown in FIG. 1, a semiconductor cleaning apparatus 100 has a
process tank 2 that holds an SPM cleaning fluid, which is a mixture of a
hydrogen peroxide solution and sulfuric acid, and is used for cleaning a
semiconductor wafer 1 (substrate) immersed in the SPM cleaning fluid,
circulation piping 4 that extends between a primary side 2a of the
process tank 2 on which the SPM cleaning fluid is injected into the
process tank 2 and a secondary side 2b of the process tank 2 on which the
SPM cleaning fluid is discharged from the process tank 2 and has a pump 3
for causing circulation of the SPM cleaning fluid, a heater 5 that is
disposed in the circulation piping 4 for heating the SPM cleaning fluid
to a predetermined temperature, a chemical injection pipe 6 for injecting
a hydrogen peroxide solution into the circulation piping 4, and a filter
7 that is disposed in the circulation piping 4 for removing particles
from the SPM cleaning fluid.
[0025] An inner tank 21 of the process tank 2 houses the semiconductor
wafer 1 and holds the SPM cleaning fluid for cleaning of the
semiconductor wafer 1. The inner tank 21 has a predetermined volume so
that the semiconductor wafer 1 can be immersed in the SPM cleaning fluid,
and the SPM cleaning fluid circulating in the circulation piping 4 is
injected into the inner tank 21 through an inlet port 8. The held SPM
cleaning fluid overflows from the inner tank 21 into an outer tank 22.
When the fluid in the outer tank 22 reaches a certain level, the pump 3
is activated to discharge the SPM cleaning fluid from a primary side 3a
to a secondary side 3b by suction, thereby causing circulation of the
chemical. Thus, the level of the SPM cleaning fluid in the inner tank 21
is kept constant.
[0026] The heater 5 controls the heating temperature of the SPM cleaning
fluid flowing thereto from a primary side 5a, thereby keeping the
temperature of the SPM cleaning fluid to be injected into the inner tank
21 at a desired temperature.
[0027] The filter 7 is disposed between the primary side 2a of the process
tank 2 and a secondary side 5b of the heater 5. The filter membrane area
of the filter 7 is larger than the cross sectional area of the
circulation piping 4, and in addition to removing particles from the SPM
cleaning fluid flowing into the filter 7 from a primary side 7a and
passing through the filter membrane, the filter 7 causes convection and
mixture of the SPM cleaning fluid before discharging the SPM cleaning
fluid from a secondary side 7b thereof.
[0028] The chemical injection pipe 6 is connected to the circulation
piping 4 at a position between the primary side 7a, which is the upstream
side, of the filter 7 and the secondary side 5b of the heater 5. The
amount of the hydrogen peroxide solution to be injected is adjusted by
opening or closing a valve 9 disposed in the chemical injection pipe 6.
By opening the valve 9, the hydrogen peroxide solution can be injected
into the circulation piping 4.
[0029] The hydrogen peroxide solution injected from the primary side 7a of
the filter 7 passes through the filter membrane, thereby being
efficiently mixed. Thus, the time from the start of injection of the
hydrogen peroxide solution into the SPM cleaning fluid until the hydrogen
peroxide concentration of the SPM cleaning fluid becomes constant can be
substantially reduced.
[0030] Furthermore, since the hydrogen peroxide solution is injected into
the circulation piping 4 in such a manner that the hydrogen peroxide
solution does not pass through the heater 5, at which the SPM cleaning
fluid circulating in the circulation piping 4 has the highest
temperature, excessive thermal decomposition and evaporation of the
hydrogen peroxide in the SPM cleaning fluid can be suppressed.
[0031] FIG. 2 shows a relationship between the hydrogen peroxide
concentration of the SPM cleaning fluid and the elapsed time from the
injection of the hydrogen peroxide at various temperatures. As shown in
FIG. 2, if the temperature of the SPM cleaning fluid is 120.degree. C.,
the hydrogen peroxide concentration remains constant, or stable, even
after a lapse of 200 seconds from the start of injection of the hydrogen
peroxide solution. If the temperature of the SPM cleaning fluid is 140
degrees Celsius, the hydrogen peroxide concentration decreases because of
thermal decomposition and evaporation after a lapse of 50 seconds from
the start of injection. Furthermore, if the temperature of the SPM
cleaning fluid is 160 degrees Celsius, which is higher than the boiling
point of hydrogen peroxide, 150 degrees Celsius, the hydrogen peroxide
concentration is low even at the peak thereof and decreases with time.
[0032] As described above, if the temperature of the SPM cleaning fluid is
equal to or higher than 120 degrees Celsius, thermal decomposition and
evaporation of hydrogen peroxide tend to easily occur. Thus, it is
essential that the SPM cleaning fluid is injected into the inner tank 21
to clean the semiconductor wafer as soon as possible after mixture, and
the SPM cleaning fluid is not excessively heated.
[0033] Thus, injecting the hydrogen peroxide solution from the chemical
injection pipe 6 into the circulation piping 4 at a position between the
primary side 7a, or the upstream side, of the filter 7 and the secondary
side 5b of the heater 5 as described above is particularly effective in
the case where the SPM cleaning fluid is heated by the heater 5 so that
the temperature of the SPM cleaning fluid in the inner tank 21 of the
process tank 2 falls within a range of 120 to 160 degrees Celsius.
[0034] FIG. 3 shows a relationship between the hydrogen peroxide
concentration of the SPM cleaning fluid in the inner tank 21 and the
elapsed time from the start of injection of the hydrogen peroxide
solution. Here, the temperature of the SPM cleaning fluid in the inner
tank 21 is 120 degrees Celsius.
[0035] As shown in FIG. 3, according to a conventional technique involving
additionally injecting the hydrogen peroxide solution into the outer tank
22, the SPM cleaning fluid is not sufficiently mixed in the outer tank
22, so that it takes about 500 seconds until the hydrogen peroxide
concentration reaches the maximum value and becomes constant. On the
other hand, according to this embodiment, the SPM cleaning solution and
the hydrogen peroxide solution additionally injected are sufficiently
mixed by the filter 7, so that the hydrogen peroxide concentration
reaches the maximum value and becomes constant in about 250 seconds,
which is a half of the time required by the conventional technique.
[0036] In addition, the maximum value of the hydrogen peroxide
concentration according to this embodiment is higher than that according
to the conventional technique. That is, according to the conventional
technique, since the SPM cleaning fluid is heated by the heater 5 after
injection of the hydrogen peroxide solution, thermal decomposition and
evaporation of the hydrogen peroxide tend to easily occur. However, it is
considered that, according to this embodiment, since injection of the
hydrogen peroxide solution occurs on the secondary side of the heater 5,
the injected hydrogen peroxide solution is not excessively heated, and
thermal decomposition and evaporation of the hydrogen peroxide are
suppressed.
[0037] Thus, a desired hydrogen peroxide concentration of the SPM cleaning
fluid can be achieved by additional injection of a smaller amount of
hydrogen peroxide solution.
[0038] As described above, the semiconductor cleaning apparatus 100
configured as described above can achieve a required resist removing
capability of the SPM cleaning fluid and optimize the amount of the
hydrogen peroxide solution additionally injected to the SPM cleaning
fluid.
[0039] A substrate cleaning method (semiconductor cleaning method) of the
semiconductor cleaning apparatus 100 configured as described above will
be described. FIG. 4 is a flowchart for illustrating a semiconductor
cleaning method according to this embodiment.
[0040] As shown in FIG. 4, first, the SPM cleaning fluid is held in the
process tank 2 for cleaning the semiconductor wafer 1 (step 1).
[0041] Then, the pump 3 is activated to cause circulation of the SPM
cleaning fluid in the circulation piping 4 extending between the primary
side 2a and the secondary side 2b of the process tank 2 (step 2).
[0042] Then, the SPM cleaning fluid is heated to a predetermined
temperature by the heater 5 disposed in the circulation piping 4 (step
3).
[0043] Then, the hydrogen peroxide solution is additionally injected from
the chemical injection pipe 6 into the circulation piping 4 at a position
between the primary side 7a of the filter 7 and the secondary side 5b of
the heater 5 where the heated SPM cleaning fluid flows (step 4). The
amount of the hydrogen peroxide solution injected is adjusted by opening
or closing the valve 9.
[0044] Then, particles in the SPM cleaning fluid are removed by the filter
7 disposed in the circulation piping 4 (step 5). By passing the SPM
cleaning fluid through the filter membrane in this step, convection of
the SPM cleaning fluid and the injected hydrogen peroxide solution
occurs, and the SPM cleaning fluid and the hydrogen peroxide solution are
sufficiently mixed before being supplied into the process tank 2.
[0045] Then, the semiconductor wafer 1 is introduced into the process tank
2 and cleaned with the SPM cleaning fluid having a predetermined
concentration set by additional injection of the hydrogen peroxide
solution (step 6). The additional injection of the hydrogen peroxide
solution may occur each time a new semiconductor wafer 1 is introduced,
or the hydrogen peroxide concentration of the SPM cleaning fluid in the
process tank 2 may be managed to inject the hydrogen peroxide solution at
an appropriate time.
[0046] As described above, in the semiconductor cleaning apparatus and the
semiconductor cleaning method according to this embodiment, the hydrogen
peroxide solution is additionally injected from the chemical injection
pipe into the circulation piping at a position between the primary side
of the filter for removing particles and the secondary side of the heater
for heating the SPM cleaning fluid to a predetermined temperature,
thereby suppressing thermal decomposition and evaporation of the hydrogen
peroxide. Thus, a required resist removing capability of the SPM cleaning
fluid can be achieved, and the amount of the hydrogen peroxide solution
additionally injected to the SPM cleaning fluid can be optimized.
Second Embodiment
[0047] With regard to the First Embodiment, there has been described a
configuration in which the chemical injection pipe for injecting the
hydrogen peroxide solution is connected to the circulation piping at a
position between the primary side of the filter for removing particles
and the secondary side of the heater for heating the SPM cleaning fluid
to a predetermined temperature. However, according to a Second Embodiment
described below, a chemical injection pipe for injecting a hydrogen
peroxide solution is connected between a primary side of a filter and a
secondary side of a heater, in particular, connected to the primary side
of the filter.
[0048] FIG. 5 shows a configuration of essential parts of a semiconductor
cleaning apparatus according to the Second Embodiment, which is an aspect
of the present invention. In this drawing, the same reference numerals as
in the First Embodiment denote the same parts in the First Embodiment.
[0049] As shown in FIG. 5, a semiconductor cleaning apparatus 200 has a
process tank 2 that holds an SPM cleaning fluid, which is a mixture of a
hydrogen peroxide solution and sulfuric acid, and is used for cleaning a
semiconductor wafer 1 immersed in the SPM cleaning fluid, circulation
piping 4 that extends between a primary side 2a of the process tank 2 on
which the SPM cleaning fluid is injected into the process tank 2 and a
secondary side 2b of the process tank 2 on which the SPM cleaning fluid
is discharged from the process tank 2 and has a pump 3 for causing
circulation of the SPM cleaning fluid, a heater 5 that is disposed in the
circulation piping 4 for heating the SPM cleaning fluid to a
predetermined temperature, a chemical injection pipe 26 for injecting a
hydrogen peroxide solution into the circulation piping 4, and a filter 7
for removing particles from the SPM cleaning fluid.
[0050] The chemical injection pipe 26 is connected to a primary side 7a of
the filter 7. The amount of the hydrogen peroxide solution to be injected
is adjusted by opening or closing a valve 29 disposed in the chemical
injection pipe 26. By opening the valve 29, the hydrogen peroxide
solution can be injected into the circulation piping 4.
[0051] As in the First Embodiment, the hydrogen peroxide solution injected
from the primary side 7a of the filter 7 is efficiently mixed by passing
through the filter membrane. Thus, the time from the start of injection
of the hydrogen peroxide solution into the SPM cleaning fluid until the
hydrogen peroxide concentration of the SPM cleaning fluid becomes
constant can be substantially reduced.
[0052] Furthermore, since the hydrogen peroxide solution is injected into
the circulation piping 4 in such a manner that the hydrogen peroxide
solution does not pass through the heater 5, at which the SPM cleaning
fluid circulating in the circulation piping 4 has the highest
temperature, excessive thermal decomposition and evaporation of the
hydrogen peroxide in the SPM cleaning fluid can be suppressed.
[0053] The semiconductor cleaning method of the semiconductor cleaning
apparatus configured described above is the same as in the First
Embodiment.
[0054] As described above, in the semiconductor cleaning apparatus and the
semiconductor cleaning method according to this embodiment, the hydrogen
peroxide solution is additionally injected from the chemical injection
pipe into the circulation piping at a position between the primary side
of the filter for removing particles and the secondary side of the heater
for heating the SPM cleaning fluid to a predetermined temperature,
thereby suppressing thermal decomposition and evaporation of the hydrogen
peroxide. Thus, a required resist removing capability of the SPM cleaning
fluid can be achieved, and the amount of the hydrogen peroxide solution
additionally injected to the SPM cleaning fluid can be optimized.
[0055] With regard to the above embodiments, there have been described
configurations in which the hydrogen peroxide solution is injected into
the circulation piping at a position between the primary side of the
filter for removing particles and the secondary side of the heater for
heating the SPM cleaning fluid to a predetermined temperature. However,
any configuration in which the
hydrogen peroxide solution is injected
into the circulation piping at least between the primary side of the
process tank and the secondary side of the heater can suppress thermal
decomposition and evaporation of hydrogen peroxide.
[0056] In addition, in the above description of the embodiments, the
substrate to be cleaned is a semiconductor wafer. However, the present
invention can be applied to other conductive or insulating substrates or
the like.
* * * * *