J. Huo et al.: Characteristics of copper films produced via atomic layer deposition
(II)-2,2,6,6-tetramethyl-3,5-heptandionate or Cu(thd)2
vapor pressure of Cu(hfac)2 и xH2O is greater than that of
the anhydrous compound. In the absence of added H2O,
dehydration by the dry carrier gas may occur. Thus it is
important to add H2O to the carrier gas stream to maxi-
mize the amount of copper delivered per pulse.10,11 It has
been shown by Lecohier et al. that an increased reaction
rate occurs even when water vapor is added to the proc-
ess chamber separately from the copper precursor, so
there is an additional benefit beyond vapor pressure en-
hancements.12 Awaya and Arita postulated that, in the
presence of water, the reaction proceeds by dissociation
of water coordinatively bonded to copper, forming oxi-
dized copper and Hhfac, followed by the reduction of
copper oxide by hydrogen.6 Lecohier et al. observed that
both hydrogen and helium carrier gases gave the same
reaction rate in the presence of water vapor on Pt seed
layer substrates, indicating that the reduction by hydro-
gen was not important.13 They proposed that the rate-
determining step was H-transfer from H2O to hfac and
that resulting OH species could be removed by combi-
nation to form H2O2 or by reaction with H2 if present.
The film growth rate observed by Lecohier et al. was
proportional to the water vapor concentration; i.e., they
operated in a regime where water vapor was the limiting
reagent. Cohen et al. clearly showed that Cu(hfac)2 de-
composes upon adsorption on a metal surface to form
Cu(hfac) and adsorbed hfac, with the latter very likely
decomposed.9
Considering the above, we propose a two-step mecha-
nism. In the first ALD step, Cu(hfac)2 и xH2O is deliv-
ered to the surface with an excess of water vapor, where
it is adsorbed and decomposed to Cu(hfac) и yH2O (y ഛ
x) and hfac, followed by reaction to form Hhfac and
oxidized copper. The reaction proceeds until the surface
is saturated with oxidized copper, hfac, and decomposi-
tion products. During the subsequent purge step, there
may be some loss of copper by reformation of Cu(hfac)2
on the surface. Hhfac has been shown to effectively react
with CuO to form Cu(hfac)2 at 200 °C.14
Reduction occurs in the second step, where reducing
gases such as alcohols transfer hydrogen to hfac on the
surface to form volatile Hhfac. They also reduce oxidized
copper to metallic copper and water. We observed that
formalin and isopropanol produce acceptable copper
films even in the absence of hydrogen. Films of about the
same thickness and resistivity are achieved on bare glass,
Si, and Si coated with TaN when H2 is replaced with Ar.
Use of hydrogen carrier gas gave a somewhat “cleaner”
looking film. Previously, in the absence of other reducing
agents, it was observed that selective deposition on Pt
seeded surfaces occurred with He carrier gas, whereas
nonselective deposition occurred with H2 as the carrier
gas.12 In the present case, the other reducing agents em-
ployed gave rise to nonselective deposition, even in the
absence of H2.
as the Cu source reduced with H2.5 However, this process
requires a layer of platinum/palladium for Cu deposition
to occur.
The Cu precursor for our current investigation is cop-
per (II)-1,1,1,5,5,5-hexafluoroacetylacetonate hydrate or
Cu (hfac)2 и xH2O. This source has been examined ex-
tensively for CVD deposition of Cu films, with process
modifications that include plasma-enhanced CVD and
addition of water or ethanol that have lead to significant
improvement in the film properties.2,6–8 To promote ef-
fective reduction of Cu(hfac)2 molecules into high-purity
copper films, the selection of external reducing agents
and film deposition conditions play extremely important
roles. Application of such reducing agents in CVD met-
allization process has been shown by Cohen et al. to
result in both increased density of Cu nuclei and faster
removal of the hfac ligands, thereby allowing for depo-
sition of smoother Cu thin films with excellent step
coverage.9
II. EXPERIMENTAL
In this investigation, we examined five different re-
ducing agents. These are methanol, ethanol, isopropyl
alcohol (IPA), formalin (approximately 37% formalde-
hyde in 10–15% methanol and water), and carbon mon-
oxide. The carrier gas for the reducing agent and
Cu(hfac)2 was H2. In the case of Cu(hfac)2, H2 was first
bubbled through water, which is an important step. Car-
bon monoxide was delivered as a 30% mixture with H2
or N2 (mixtures were supplied by Air Liquide, Morris-
ville, PA). The Cu films were deposited on 50 × 50 mm
substrates that included glass plates and silicon wafers
pre-coated with a 500-nm layer of SiO2, followed by a
barrier layer about 6 nm thick. The three different barrier
layers examined were Ta, TaN, and TiN.
The Cu deposition was performed in a microchemistry
F-120 ALD reactor. A typical ALD cycle consisted of a
1.5-s-long Cu(hfac)2 pulse, then a 1.2-s N2 purge, fol-
lowed by a 1-s reducing agent pulse, and finally another
1.2-s N2 purge. The Cu source was heated to 75 °C, and
the reducing agents were all at room temperature. The
chamber pressure was 5 mtorr. Although deposition of
Cu was observed in all cases around 230 °C, the results
reported here were produced at 300 °C, unless other-
wise noted.
III. PROPOSED MECHANISM
As mentioned previously, the carrier gas for the
Cu(hfac)2 was H2 that was first bubbled through water.
The importance of water has been studied rather exten-
sively for CVD deposition of Cu from Cu(hfac)2. The
J. Mater. Res., Vol. 17, No. 9, Sep 2002
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