Modeling of Reverse Tone Etchback Shallow Trench Isolation
Chemical Mechanical Polishing
Terence Gan,
a
Tamba Tugbawa,
a
Brian Lee,
a,
* Duane S. Boning,
a,
**
,z
and Simon Jang
b
a
Microsystems Technology Laboratories, Massachusetts Institute of Technology, Cambridge,
Massachusetts 02139, USA
b
Taiwan Semiconductor Manufacturing Company, Hsin-Chu, Taiwan
In this paper, we introduce a mathematical model for chemical mechanical polishing CMP of reverse tone etchback shallow
trench isolation STI structures. We present a detailed formulation of the model and describe CMP experiments using a newly
designed STI CMP characterization mask to validate the model. A methodology for extracting the model parameters is also
proposed. An improved modeling methodology that incorporates density averaging effects fits the experimental data more accu-
rately. Finally, we use the model to predict the effects of pre-CMP step height, pattern density, polish time, pad hardness, and
slurry selectivity on dishing and nitride erosion.
© 2001 The Electrochemical Society. DOI: 10.1149/1.1348266 All rights reserved.
Manuscript submitted June 1, 2000; revised manuscript received November 21, 2000.
Shallow trench isolation STI is an enabling process for ad-
vanced ultralarge scale integration ULSI technologies. It can be
scaled to fine dimensions while maintaining good planarity, good
latch-up immunity, and low junction capacitance.
1,2
However, the
chemical mechanical polishing CMP process is density
dependent,
3,4
and single-step STI CMP can lead to significant oxide
dishing and nitride erosion problems. Hence, an additional etchback
step is commonly used before CMP to remove the overburden oxide
over large active areas. The resulting CMP process is concerned
only with removing the excess oxide in the trenches until the oxide
reaches the same level as the nitride. This is a complicated process
that depends on the relative removal rate of the oxide in the trenches
and the nitride barrier in the raised area, which are both density
dependent. There are currently no existing models for reverse tone
etchback STI CMP, even though models for single-step STI CMP
5
and process control methods exist.
6
In this work, a mathematical
model for reverse tone etchback STI CMP based on density and step
height dependent oxide and nitride removal rates is presented.
The model presented here builds on previous work. Stine et al.
demonstrated the strong relationship between CMP removal rate and
pattern density.
3
Smith et al. described integrated pattern density
and step height models for oxide CMP.
7
Tugbawa et al. developed a
removal rate vs. step height model for dual-material damascene
CMP.
8
The reverse tone etchback STI CMP model presented here is
an adaptation of Tugbawa et al.’s dual-material damascene CMP
model, which greatly simplifies the analysis of reverse tone etchback
STI CMP.
Model Formulation
Chemical mechanical polishing achieves global planarity through
a combination of chemical action from the slurry and mechanical
action from the polishing pad and slurry particles. The slurry chem-
istry can be adjusted for varying degrees of selectivity between dif-
ferent materials, but the contact between the polishing pad and the
wafer is believed to be the main mechanism for removing the local
step height to accomplish planarization. In STI CMP, we are inter-
ested in changes in step height especially dishing and nitride ero-
sion. This makes a step height based model a convenient starting
point. When analyzing step height changes, we are not concerned
with the details of the physical or chemical aspects of CMP; instead,
we seek an effective and efficient model capturing the net effect of
all contributing factors. From the measurement point of view,
changes in local step height are easily made and used here to de-
velop and confirm the STI CMP model.
Figure 1 shows the cross section of a reverse tone etchback wafer
before and after CMP, and we use it to define step height and nitride
erosion as follows. The local step height is the vertical distance
between the top of the nitride and the top of the oxide. It is positive
when the oxide is above the nitride, and negative when the oxide
recesses below the nitride. Negative step height is also known as
dishing. Nitride erosion is simply the amount of nitride loss due to
CMP.
The model is explained graphically in Fig. 2, which shows how
the oxide and nitride removal rates on a reverse tone etchback STI
wafer change with step height. Polishing progresses from the right
to the left of the graph as indicated by the arrows. Following the
work of Grillaert et al.,
9
if the initial local step height is very large,
the pad will not contact the down area nitride initially, and there
will be no down area polishing. The up area oxide polish rate is
density dependent and is given by the expression RR
ox
= K
ox
/1
- , where K
ox
is the blanket oxide removal rate, and is the nitride
density. As the wafer polishes, only the up areas are polished and
this causes the local step height to decrease. At some critical step
height denoted by d
max
, the pad just touches the down area. Addi-
tional polishing further reduces the local step height which increases
the force of contact between the pad and the down area while it
decreases the force between the pad and the up area. This causes the
down area removal rate to increase and the up area removal rate to
decrease. For simplicity, the model assumes that the down area re-
moval rate increases linearly and the up area removal rate decreases
linearly with decreasing step height. When the local step height is
zero, we postulate that the down area removal rate is equal to K
nit
,
the blanket nitride removal rate. Similarly, the up area polish rate is
equal to K
ox
, the blanket oxide removal rate. Overpolishing causes
dishing to occur. As long as the oxide removal rate is higher than the
nitride removal rate, the amount of dishing increases with polish
time. Eventually, the oxide removal rate and nitride removal rate
become equal and steady-state dishing occurs. We denote this point
by d
ss
.
From Fig. 2 we can formulate the equations for the oxide and
nitride removal rates as follows
Oxide removal rate
RR
ox
=
K
ox
1 -
H d
max
K
ox
1 +
1 -
H
d
max
-d
ss
H d
max
1
* Electrochemical Society Student Member.
** Electrochemical Society Active Member.
z
E-mail: boning@mtl.mit.edu
Journal of The Electrochemical Society, 148 3 G159-G165 2001
0013-4651/2001/1483/G159/7/$7.00 © The Electrochemical Society, Inc.
G159