Removing
gold seed-layer materials using reactive ion etch
Paul
Werbaneth, Tegal; and Tim Lester and Jadwiga Pakulska, Nortel Networks
A
variety of metals can be used for interconnect metallization in IC and
MEMS device fabrication. Aluminum and aluminum alloys, tungsten, copper,
platinum, and gold are all employed as thin-film conductors in microelectronic
device fabrication. Manufacturers choose which material to use for specific
applications based on the many different electrical and mechanical properties
that must be optimized to fabricate conductor layers or to perform interconnect
tasks. These essential properties include film electrical resistivity,
mechanical and chemical stability, adhesion characteristics, film deposition
characteristics, and the ease with which films can be patterned. When
used as interconnect materials, copper and gold have several notable
performance advantages: they offer low resistivity (1.7 µΩ-cm
and 2.2 µΩ-cm, respectively) and prevent electromigration-related
failures.1 To ameliorate resistance-capacitance delay issues,
which degrade overall device performance, copper is widely used as the
material of choice for interconnects in leading-edge CMOS ICs.
While
gold is seldom used for interconnect metallization in silicon-based
devices (except in backside metallization processes), it is used extensively
in MEMS and compound semiconductor device fabrication and in wafer packaging
applications because of its high electrical conductivity and its relative
chemical inertness.2 Gold interconnects are also compatible
with the semiconductor contact metallurgies and gate metal stacks typically
used in compound semiconductor devices.
Typical
gold thicknesses used in MEMS, compound semiconductor, and packaging
applications are 3, 2030, or 4.5 µm.35 Generally,
gold is deposited on top of an adhesion-promoting or a diffusion barrier
layer commonly composed of titanium, tungsten, or platinum. Since electroplating
achieves excellent pattern fidelity while conserving the expensive starting
material, it is the standard method for depositing gold films. Consequently,
in addition to adhesion-promoting and diffusion barrier layers, a thin
layer of gold or platinum seed metal is almost always deposited before
the bulk of the gold is electroplated. On normal topographies, at least
100 nm of seed metal are required to achieve low resistance and uniform
plating.
Since
the goal of the interconnect process is to form independent, distinct,
electrically isolated conductive lines of gold, one of the final process
steps in an electroplated gold interconnect process module, after electroplating
has occurred and the electroplating mask has been stripped, is the removal
of the seed layer and the diffusion barrier/adhesion-promoting stack.
Removal of this electrically conductive metal stack effectively isolates
the metal interconnect lines formed during electroplating, freeing them
to perform their designated tasks. Figure 1 shows a schematic of an
electroplated structure before and after the etching of the seed layer.
 |
| Figure 1: Schematic diagrams of
electroplated structure (a) before and (b) after seed-layer etch. |
Fabricating
gold-plated interconnects in compound semiconductors often does not
require a barrier layer, but adhesion promotion is still important.
For example, in some cases a 10-nm titanium adhesion layer followed
by 100 nm of gold deposited by evaporation or sputtering would be sufficient
to perform the plating process. In practice, however, a more-complex
seed-layer stack (i.e., the entire seed layer/diffusion barrier/adhesion-promoting
stack) may be required to overcome problems encountered during the seed-layer
removal process.
Several
standard techniques are available for removing seed layers following
electrodeposition, each of which has characteristic strengths and weaknesses
that come to light when seed-layer film removal processes are employed
in volume production. Three such methods are wet processing, reverse
plating, and reactive ion etch (RIE). This article demonstrates that
the use of RIE to remove seed-layer materials is an attractive alternative
to the other standard methods. It highlights the important differences
between the approaches and demonstrates that RIE in a high-density plasma
reactor is more effective than the other techniques for removing gold
seed layers.
Wet
Processing
Wet
processing is commonly used to remove gold seed layers from MEMS and
compound semiconductor devices. However, while wet processing can remove
seed layers, it undercuts the plated gold line (possibly reducing its
mechanical integrity), does not remove the layer uniformly, causes excessive
loss of plated metal, raises environmental and safety issues related
to the use of wet-etch chemistries, and is expensive.
Early
attempts at Nortel Networks (Nepean, ON, Canada) to remove a simple
Ti/Au seed layer by wet etching proved unsuccessful. It was found that
both potassium iodide (KI)based etches and commercially available
cyanide-based chemistries etched the plated gold two to three times
faster than the evaporated or sputtered seed gold. The plated metal
also became very rough as its grain structure was delineated. That result
prompted an investigation into the use of reverse plating to remove
the gold portion of the seed layer.
Reverse
Plating
In
order to remove the gold portion of the seed layer by reverse plating,
an underlying conductive layer is required to supply the current. In
the absence of such a layer, nonuniform removal rates cause traces of
seed layer to be left in regions that become disconnected electrically
from the contacts at the periphery of the wafer. Therefore, the adhesion/barrier
portion of the seed layer stack must be able to function independently
as a reliable conducting layer over any existing topography. That layer
must be removed by means of a separate process step.
Reverse
plating is generally performed at constant current, and the voltage
can be monitored to detect the endpoint. In early reverse-plating efforts
at Nortel, the wafer was clipped onto a polypropylene plate using eight
contacting clips and then fully immersed in a recirculating bath. Subsequently,
the process was carried out in an automated single-wafer system that
incorporated a fountain deplate head and a rotating wafer holder with
pins that gripped the edge of the wafer and contacted the seed layer.
As recommended by the tool manufacturer, only one electrolyte (a solution
of thiourea, NH2CSNH2) was
investigated.
 |
| Figure 2: SEM images of center
and edge of wafer with (a) reverse plating time optimized for the
wafer center, and (b) excessive etching of the metal feature at
wafer edge. |
The
Gold Reverse-Plating Process. Unlike wet etching, reverse plating
removes the seed gold at about the same rate as the plated gold. However,
the gold continues to be electrochemically etched once the underlying
conducting layer has been reached. In fact, experiments found that at
a constant current, the removal rate of the plated gold lines increases
significantly once most of the gold seed layer has been cleared. That
effect is severe for isolated features, where the nonuniformity of the
reverse-plating process becomes a critical issue. As shown in the SEM
images in Figure 2, when reverse-plating time is optimized for the center
of the wafer, the edge experiences excessive etching.
To
complicate matters, interconnect lines in compound semiconductor circuits
are typically many microns thick, and the seed-layer removal rate is
slightly lower in the high-aspect-ratio gap between two closely spaced
metal lines. Consequently, an extended reverse-plating step is required
to clear these regions, which also results in excessive removal of the
plated lines.
 |
| Figure 3: Reverse-plating endpoint
traces for three different metal patterns (product codes). |
Typical
endpoint signals during reverse plating are presented in Figure 3. Even
after deplate uniformity has been optimized, endpoints are not very
abrupt and can vary significantly with the overall density of the interconnect
on the wafer. Overall, there is very little process margin for reverse
plating of the seed layer. Therefore, extended deplate times must be
fine-tuned for different metal patterns (product codes).
Increasing
the Thickness of the Titanium Adhesion Layer. Increasing the thickness
of the titanium adhesion layer to 30 nm can provide the needed conduction
to reverse-plate the gold. However, great care must be taken not to
create breaks in this layer, particularly at the die periphery, where
scribe line etches can create large amounts of topography. At Nortel,
the investigators found that replacing hot O2
downstream ashing of the plating resist with wet strips and a room-temperature
O2 descum procedure in a parallel-plate RIE tool
can prevent such breaks.
The
remaining thin titanium layer can be removed using wet chemical etching
in hot phosphoric acid, or dry etching with fluorine- or chlorine-containing
plasmas. Wet etching of a simple titanium base layer is problematic.
A frilly, very tenuous network of seed layer, caused by the diffusion
of gold into the grain boundaries of the titanium, often remains after
etching, requiring that a final dilute KI gold etch be performed to
remove the frills. Since Ti/W sputtered from a compound target does
not suffer from the gold diffusion problem, it can be etched away cleanly
in 60°C peroxide. Unfortunately, it was found that Ti/W has a tendency
to undercut, as illustrated in the SEM images in Figure 4. On occasion,
such undercutting was severe enough to cause the narrow interconnect
lines to lift.
 |
| Figure 4: Undercutting of TiW layer
after H2O2 wet etch. |
In
contrast, dry etching offers the advantage of reducing Ti layer undercutting,
but it can cause stringers to remain along vertical edges or grooves
in the underlying topography because of the directionality of the etch.
Initial attempts to dry etch the titanium adhesion layer eventually
prompted Nortel to adopt the method of planarizing the underlying topography
to prevent residual stringers.
 |
Figure 5: Diagram of the dual-frequency,
high-density plasma reactor.
|
Using
RIE to Remove Seed Layers
Plasma
Reactor Configuration. The limitations of using wet processing or
reverse plating to remove the seed-layer from compound semiconductor
devices led Nortel to investigate the use of plasma reactors for seed-layer
removal. The work discussed in this article was performed using a 6520
dual-frequency plasma reactor from Tegal (Petaluma, CA). The reactor
is illustrated in Figure 5, and a top view of the system platform showing
two etch reactors, a plasma strip module, and a wet-rinse station is
shown in Figure 6.
 |
| Figure 6: Top-view diagram of the
plasma reactor system platform, showing two etch reactors, an inductively
coupled plasma (ICP) strip module, and a wet-rinse station. |
Once
Nortel had decided that dry etching would be successful if the topography
underneath the seed layer were planarized to eradicate residual stringers,
a process using high-density-plasma etching of the full seed-layer stack
was considered. Work at Tegal had already resulted in the successful
pattern etching of platinum and gold layers using a version of the high-density
plasma reactor shown in Figures 5 and 6. Work at Nortel qualified the
reactor for dry etching of seed-layer metals. That qualification resulted
from tests to determine the etch rate of exposed metals during other
compound semiconductor plasma etching steps. Only a few samples were
etched because of chamber contamination concerns, but preliminary results
indicated that the reactor could be used successfully to etch the gold
portion of a seed layer and that it might also be able to handle thin
platinum layers, as indicated in Figure 7.
 |
Figure 7: RIE plasma etch rates
of various isolated metal features on a GaAs substrate.
|
The
plasma etch of gold and platinum generally relies on a strong physical
etch component provided by surface bombardment of the wafer with energetic
ions from the plasma, and a reactive etch component (chiefly halogen
radicals created in the plasma).6, 7 Table I lists the elements
most often found in seed-layer stacks and the halogens used to etch
them in plasma reactors. Since titanium and tungsten etch readily in
fluorine chemistries without much ion bombardment, the plasma reactor
used to etch different films must be optimized in order to achieve independent
control of plasma density and ion bombardment energy.8
|
Element
|
Etchant
(Plasma Reactor)
|
|
Gold
|
Fluorine,
chlorine, bromine
|
|
Platinum
|
Chlorine,
bromine
|
|
Titanium
|
Fluorine,
chlorine
|
|
Tungsten
|
Fluorine,
chlorine
|
|
| Table I: Plasma etchants for seed-layer
metals. |
Using
chlorine- and bromine-based etchants requires that the plasma reactor
be isolated from the atmosphere with vacuum loadlocks. The reactants
and the product compounds formed during plasma etching inevitably adhere
to the walls of the plasma reactor. Should the reactor be exposed to
a moist atmosphere between etches, the deposits on the reactor walls
hydrolyze, resulting in the generation of potentially harmful vapors
that can cause wafer-to-wafer process instability and particle-related
defects. Chlorinated etch chemistries can also result in postetch corrosion.
There
are many well-established techniques for preventing postetch corrosion
in etched films. Usually, residual chlorine is removed immediately after
etch by exposing the wafer to oxygen- or hydrogen-containing plasmas,
heating the wafer under vacuum, rinsing the wafer with DI water or another
aqueous solution, or performing some combination of these techniques.
 |
| Figure 8: With power set at 40
W kHz, the etching of the seed layer (consisting of a 10-nm-thick
titanium film and 100-nm-thick gold film) was not clean. Resputtered
metal was left on the sides of the metal lines and the seed metal
on the more sloped portion of the topography was not removed adequately. |
Experimental
Results. The tests discussed here focused on the use of a Cl2/helium
gas mixture with or without the addition of argon. All the work was
done at a fixed megahertz power setting and a fixed pressure of <10
mTorr. Initial observations indicated that even though the gold etch
rate was quite high when power was set at 40 W kHz, the etching of the
seed layer (which consisted of a 10-nm-thick titanium film and 100-nm-thick
gold film) was not clean at that bias power level. Resputtered metal
was left clinging to the sides of the metal lines, and the seed metal
on the more sloped portion of the topography was not removed adequately,
as illustrated in the SEM image in Figure 8. Figures
9a9c show the improvement in seed-layer removal as power was
increased to 60, 70, and 80 W kHz, respectively.
It
was also found that at higher kilohertz powers, the amount of overetch
required to avoid leaving metal stringers was directly related to the
vertical thickness of the seed metal on sloped surfaces that had a maximum
angle of about 60° from the horizontal surface. For steeper slopes,
the results varied considerably. Since the thickness of seed layers
deposited by sputtering is quite uniform over smoothed topographies,
a slope of 60° or less requires that seed layer overetch be at
least 100%.
A
major concern was that as more wafers were run in the chamber, the surface
leakage between lines could increase as a result of resputtering from
the accumulated chamber deposits. Consequently, a special structure
was included in the process control monitor to test for interline leakage.
That structure was composed of interleaved fingers of a minimum-line-width
plated metal at minimum pitch that was placed over a random underlying
topography. Because the leakage current between the fingers after etch
and a water rinse was not negligible, a special postetch treatment was
devised to reduce the leakage to a level comparable to that of the reverse
plating process. Subsequently, as more wafers were etched in the chamber,
the leakage abated, causing no noticeable change in the appearance of
the interconnect.
Since
gold chloride etch products are not very volatile at moderate etching
temperatures, it was anticipated that a successful production process
would require a good chamber-clean strategy. Thus, removable ceramic
shielding developed by Tegal was installed in Nortel's 6520 reactor.
With increased shielding in place, nearly all of the chamber surfaces
exposed to direct-line-of-sight coatings were protected. However, the
installation of the redesigned ceramic liner produced a marked leakage
spike, illustrating the need to condition new ceramic shields before
they are used for production. After undergoing conditioning, the additional
shielding did not alter the etch characteristics of the chamber.
The
first chamber clean was triggered not by a degradation in the seed-layer
etch, but by the tool's inability to detect plasma ignition because
of deposits on the endpoint sensor window. Therefore, a dilute aqua
regia etch (15 HCl:15 HNO3:70 H2O)
was used to etch the gold deposits off tool windows and ceramic parts.
When the chamber was returned to service, a very small increase in test-structure
leakage current was noticed. After several more wafers were etched,
however, the current returned to its normal value, as shown in Figure
10.
 |
| Figure 10: Postetch test structure
leakage current measurements from the plasma chamber's metal isolation
test structure. (The wafer count is approximate and does not include
test and setup wafers. Values are wafer medians.) |
Conclusion
Several
standard techniques used to remove gold seed-layer films from electroplated
metallization structures created during compound semiconductor device
fabrication have been examined. Wet etching of the seed layer was found
to be impractical because it causes excessive etching of the plated
metal features and undercuts the adhesion or barrier layer. Reverse
plating is too dependent on overall pattern density, making it impractical
for use in a volume production fabrication line running many different
product codes. The reverse-plating process also exhibits a significant
loading effect; as the seed layer clears, there is a marked increase
in the rate at which gold in the interconnect lines is removed, making
the reverse-plating process difficult to control.
The
work reported in this article on the optimization of seed-layer etching
demonstrates that reactive ion etching of seed-layer materials is an
excellent alternative to wet etch or reverse plating methods. Robust
processes with high etch rates, good throughputs, and good electrical
results can be optimized in low-pressure, high-density-plasma reactors
with good repeatability over many etched wafers.
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Paul
Werbaneth is a regional marketing director at Tegal (Petaluma, CA).
He has worked for more than 20 years in semiconductor process engineering
and technical marketing positions at Intel, Hitachi America, and Tegal.
Werbaneth is the author or coauthor of more than 35 papers and articles
on all aspects of plasma etch processing. He is a member of AVS, ECS,
IEEE, and SPIE, and is on the GaAs Mantech Technical Program Committee,
the SEMI International MEMS Advisory Group, and the steering committee
of the Advanced Semiconductor Manufacturing Conference. He received
a BS in chemical engineering from Cornell University in 1979. (Werbaneth
can be reached at 707/765-5608 or pwerbane@tegal.com.)
Tim
Lester, PhD, is a senior member of the scientific staff at Nortel
Networks (Nepean, ON, Canada), where he has spent most of his career
as part of the high-speed-modules development group. He is responsible
for the design and integration of processes for the manufacture of gallium
arsenide and indium phosphide heterojunction bipolar transistors. He
has a BS in physics from the University of Victoria, BC, Canada, and
an MS in astronomy and a PhD in solid-state electronics from the University
of British Columbia, Canada. (Lester can be reached at 613/763-5923
or tlester@nortelnetworks.com.)
Jadwiga
Pakulska, PhD, works for the optoelectronics and microelectronics
groups of Nortel Networks, where she is responsible for gold electrodeposition
of metal interconnects for III-V semiconductor devices. She received
an MS from Adam Mickiewicz University in Poznan, Poland, in 1974 and
a PhD from Wroclaw Technical University, Poland, in 1984 for studies
of thin oxide films on metal alloys. (Pakulska can be reached at 613/763-3610
or jadwiga@nortelnetworks.com.)