Information
-
Patent Grant
-
6280079
-
Patent Number
6,280,079
-
Date Filed
Thursday, December 24, 199826 years ago
-
Date Issued
Tuesday, August 28, 200123 years ago
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Inventors
-
Original Assignees
-
Examiners
Agents
- Thomas, Kayden, Horstemeyer & Risley, LLP
-
CPC
-
US Classifications
Field of Search
US
- 366 1651
- 366 1653
- 366 1654
- 366 1655
- 366 1682
- 366 280
- 366 315
- 366 317
- 366 32592
- 366 32593
- 366 262
- 366 263
- 366 270
- 366 274
- 366 348
- 366 1591
- 366 265
- 366 343
- 451 446
- 451 60
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International Classifications
-
Abstract
A slurry mixing apparatus has a mixing chamber, a rotatable bearing and several blades. The bearing is connected to one end of each of the blades and located in the center of the mixing chamber. Several kinds of the slurries can be mixed rapidly in the apparatus and flowed into the CMP polisher immediately to perform a CMP process. Being mixed by the mixing chamber, the slurry is supplied to the chemical mechanical polisher for polishing.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates to chemical mechanical polishing (CMP) polisher and more particularly to a slurry mixing apparatus for the CMP polisher.
2. Description of the Related Art
Planarization is an important technology in semiconductor process. The surface of the wafer has an even topography after planarization and it is able to prevent exposure light source from being scattered, so that the pattern transfer can be carried out precisely. Planarization technology mainly includes two methods, spin-on glass (SOG) and chemical mechanical polishing (CMP). SOG can not satisfy gradually the requirement of planarization as the semiconductor technique enters the field of sub-half-micron. CMP is the only process currently that can provide global planarization in very-large scale integration (VLSI) and ultra-large scale integration (ULSI).
CMP is a planarization process to planarize an uneven surface by applying mechanical polishing and adding suitable chemical reagent and slurry. When conditional parameters of process can be controlled appropriately, the planarization degree may reach 94% by CMP. Referring to FIG.
1
and
FIG. 2
, schematic top view and side view of a CMP polisher known in prior art are shown respectively. A holder
102
holds a backside
106
of a wafer
112
, and a front side
120
of the wafer
112
is facing a polish pad
114
on a polish table
100
. A slurry
110
from a slurry supplier
118
is pumped into a pipe
104
by a pump
116
, and thus, the slurry
110
can be supplied to the polish pad
114
continually. The chemical reagent in the slurry
110
is reacted with the front side
120
of the wafer
112
, and the polish table
100
and the holder
102
are rotated along directions
108
a,
108
b
to polish the wafer
112
mechanically by particles in the slurry
110
. Chemical reaction and mechanical polishing are repetitively applied on the wafer, and an even surface can be therefore obtained by the planarized process of CMP.
The quality of the slurry determines the stability of the process, so it is important in the planarized process of CMP. Chemical reaction and mechanical polishing are decided by chemical reagent and particles in the slurry respectively. The slurry needs to be diluted by solvent and then can be used, so that the slurry is varied from different materials and it is often necessary to use two kinds of slurry to planarized the wafer.
Since the slurry needs to be diluted to a suitable concentration, a premixer (not shown) is added in the slurry supplier
118
to mix slurry in advance. However, the property of the slurry is easily varied after being mixed. Thus, the slurry has to be consumed after being mixed and before reaching a Pot life. Due to the instability of the mixed slurry, another in-situ slurry mixing apparatus is developed due to the unstable property of the pre-mixed slurry.
Referring to
FIG. 3
, it shows a side view of an in-situ slurry mixing apparatus in prior art. The in-situ slurry mixing apparatus includes a pipe
202
, a pipe
204
(in order to simplify the illustration, only pipes
202
,
204
are shown in
FIG. 3
) and a slurry pipe
206
. Different slurries are pumped into the slurry pipe
206
through the direction shown as arrow
202
a,
204
a
from pipes
202
,
204
. The slurry in the slurry pipe
206
is directly provided onto the polished pad (such as
110
shown in
FIG. 2
) along the direction of the arrow
206
a.
However, the mixing time of the in-situ slurry mixing apparatus is too short to cause nonuniformity of the slurry, so that the quality of the slurry can not be easily controlled and result in worse performance of CMP.
SUMMARY OF THE INVENTION
It is therefore an object of the invention to provide a slurry mixing apparatus for the CMP polisher. The slurry mixing apparatus solves the problem of time-varying-property of the pre-mixing slurry.
It is another object of the invention to provide a slurry mixing apparatus for the CMP polisher. The slurry mixing apparatus solves the problem of nonuniform mixed slurry from the in-situ slurry mixing apparatus.
To achieve these objects and advantages, and in accordance with the purpose of the invention, as embodied and broadly described herein, the invention is directed towards a slurry mixing apparatus. The apparatus includes a mixing chamber, a rotatable bearing and several blades. The bearing is connected to the blades and installed in the mixing chamber. Several kinds of the slurries can be mixed rapidly in the apparatus and flowed into the CMP polisher immediately to perform a CMP process. The disadvantage of property of pre-mixing slurry being varied from time can be solved and the problem of nonuniform slurry due to in-situ slurry mixing can be overcome. The quality of the mixing slurry is thus improved.
It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are not restrictive of the invention as claimed.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG.
1
and
FIG. 2
are schematic top view and side view of planarized process apparatus for CMP known in prior art;
FIG. 3
is a cross sectional view of the in-situ slurry mixing apparatus known in prior art;
FIG. 4
shows schematic view of a slurry mixing apparatus according to the invention; and
FIG. 5
shows schematic side view of a slurry mixing apparatus according to the invention.
FIG. 6
shows a schematic side view of a slurry mixing apparatus similar to that shown in
FIG. 5
, except having flat blades.
FIG. 7
shows a schematic side view of a slurry mixing apparatus similar to that show in
FIG. 5
, except having blades curved in a counterclockwise direction.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
FIG.
4
and
FIG. 5
show respectively schematic top view and side view of a slurry mixing apparatus according to the invention. The apparatus includes a mixing chamber
300
having a surrounding wall
322
, a rotatable bearing
312
located at a central point of the mixing chamber, and several stirring blades
310
each with one end connected to the rotatable bearing
312
, the other end close to the surrounding wall
322
. Both the rotatable bearing the stirring blades are enclosed by the surrounding wall
322
. The stirring blades
310
may be shaped embowed, curved, or flat. The mixing chamber
300
also includes a slurry input pipe
302
and a slurry output pipe
304
to transport a slurry in and out of the mixing chamber
300
.
The slurry input pipe
302
and the slurry output pipe
304
are connected to the mixing chamber
300
through the surrounding wall
322
. The slurry input pipe
302
is further connected to a supplying pipe
306
with the other end. While the slurry is input to the mixing chamber
300
via the slurry input pipe
302
with a direction shown as arrow
302
a,
the blades
310
are rotating and sliding through an interior surface of the surrounding wall
322
. The slurry output pipe
304
is connected to the mixing chamber
300
with one end, and with the other end outputting the slurry to the CMP polisher with a direction shown as arrow
304
a
(shown as FIG.
1
A and FIG.
1
B). Referring to
FIG. 5
, several kinds of the slurry materials are pumped into the slurry input pipe
304
through the pipes
306
,
308
along the direction of the arrow directions
306
a,
308
a
and continuously enter the mixing chamber
300
. When the slurry enters the mixing chamber
300
and beat one of the blades
310
, the slurry flow is swirled along the direction shown as the arrow
318
, and the blades
310
are accelerated and driven by the slurry. As a consequence, the blades
310
rotate along the direction shown as the arrow
320
. By rotating the blades
310
, the slurry is carried and stirred by the blades
310
. While the slurry is carried towards the slurry output pipe
304
, an evenly mixed slurry is obtained and supplied to the chemical mechanical polisher. As shown in the figure, the blades
310
are curved in a clockwise direction. It is appreciated that other shapes, for example, curved in a counterclockwise direction, or flat shape, may also be applied to achieve the evenly mixing purpose. Furthermore, in this embodiment, the blades
310
are rotating in a counterclockwise direction as shown as the arrow
320
. While the locations of the slurry input pipe
302
and the slurry output pipe
304
are interchanged, the blades
310
are then rotating in an opposite direction, that is, a clockwise direction.
The size of the slurry input pipe
302
is about {fraction (1/100)} of the size of the mixing chamber
300
. For example, while the diameter of the mixing chamber
300
is 3 inches, the diameter of the slurry input pipe is about 0.03 inch. The mixing chamber
300
is made of acid-base-resistant material, such as TEFLON, PFMA (Polyfluorinated methacrylate) or the likes. The material of the blades
310
includes acid- and base-resistant material, for example, TEFLON, PFMA or the likes.
The slurry mixing apparatus in
FIG. 4
only shows one slurry input pipe
302
and one slurry output pipe
304
. In the practical application, the slurry mixing apparatus may comprises more than one slurry input/output pipes, that is, one slurry output pipes and several slurry inputs, several slurry output pipes and one slurry input pipes, or even several input pipes and slurry output pipes as specifically required.
Since the slurry is pumped into the mixing chamber
300
through the slurry input
314
and the blades
310
are rotated to stir the slurry to induce convolution of the slurry, the slurry is thus evenly mixed inside of the mixing chamber
300
. In addition, while performing polishing, fresh mixing slurry is continuously pumped into the slurry input pipe
302
and the flows into the CMP polisher. The slurry supplying to the chemical mechanical polisher is therefore uniform and fresh, so that the property of the slurry does not vary with time. The problem of time varying property of the slurry in the conventional pre-mixing process can be solved. Therefore, the chemical mechanical polishing process can be more stable than that in prior art. The problem of short mixing time of in-situ slurry mixing apparatus in prior art can be overcome by this invention. The property of the slurry is easily controlled to enhance the performance of the CMP.
Reference is made briefly to
FIG. 6
, which shows a schematic side view of a slurry mixing apparatus similar to that shown in
FIG. 5
, except having flat blades. In this regard, the reference numbers for the apparatus of
FIG. 6
are similar to
FIG. 5
, except that the leading digit has been changed from “3” to “4”. With regard to the mechanics of operation, the slurry mixing apparatus of
FIG. 6
operates similar to that of
FIG. 5
, therefore no further discussion need be provided.
Reference is made briefly to
FIG. 7
, which shows a schematic side view of a slurry mixing apparatus similar to that shown in
FIG. 5
, except having flat blades. In this regard, the reference numbers for the apparatus of
FIG. 7
are similar to
FIG. 5
, except that the leading digit has been changed from “3” to “5”. With regard to the mechanics of operation, the slurry mixing apparatus of
FIG. 7
operates similar to that of
FIG. 5
, therefore no further discussion needs to be provided.
As described above, the features of this invention include:
1. Since the slurry is pumped into the mixing chamber through the slurry input pipe, and the slurry is swirled while beating by the blades. The slurry is thus carried, mixed, and stirred by the blades, so that a uniformly mixed slurry is obtained and supplied for the polishing process. As a consequence, the performance of CMP is enhanced.
2. Since fresh slurry is pumped into the mixing chamber continuously, and the uniformly mixed slurry is supplied to the CMP polisher, the property of the mixing slurry does not vary form time and the CMP process is more stable.
3. The apparatus of the invention is compatible with the current CMP polisher, so that there is no problem for implementing the apparatus into the current CMP polisher for manufacturing.
Other embodiment of the invention will appear to those skilled in the art from consideration of the specification and practice of the invention disclosed herein. It is intended that the specification and examples to be considered as exemplary only, with a true scope and spirit of the invention being indicated by the following claims.
Claims
- 1. A method for mixing slurries used in a chemical mechanical polisher, comprising:inputting slurries into a mixing chamber, wherein the mixing chamber comprises a plurality of blades and a bearing, and the blades are connected to the bearing; driving the blades with a force from the introduction of the slurries into the mixing chamber; stirring the slurries by the rotating blades to mix the slurries; and outputting the slurries into a chemical mechanical polisher.
- 2. The method of claim 1, wherein the step of stirring the slurries by the rotating blades comprises stirring the slurries by the rotating blades with an embowed shape.
- 3. The method of claim 1, wherein the step of stirring the slurries by the rotating blades comprises stirring the slurries by the rotating blades curved in a clockwise direction.
- 4. The method of claim 1, wherein the step of stirring the slurries by the rotating blades comprises stirring the slurries by the rotating blades curved in a counterclockwise direction.
- 5. The method of claim 1, wherein the step of stirring the slurries by the rotating blades comprises stirring the slurries by the rotating blades in a flat shape.
- 6. The method of claim 1, further comprising the step of sliding the blades along an interior surface of the mixing chamber.
- 7. The method of claim 1, wherein the step of inputting slurries into a mixing chamber comprises inputting slurries into a mixing chamber made of TEFLON.
- 8. The method of claim 1, wherein the step of inputting slurries into a mixing chamber comprises inputting slurries into a mixing chamber made of TEFLON.
US Referenced Citations (23)