Glycolic acid in hydrogen peroxide-based slurry for
enhancing copper chemical mechanical polishing
Tzu-Hsuan Tsai
a,*, Yung-Fu Wu
b, Shi-Chern Yen
ba
Department of Chemical Engineering, Northern Taiwan Institute of Science and Technology, No. 2, Xueyuan Rd., Beitou, Taipei 112, Taiwan, R.O.C.
bDepartment of Chemical Engineering, National Taiwan University, Taipei 106, Taiwan Received 14 August 2004; accepted 30 October 2004
Available online 19 November 2004
Abstract
The effects of glycolic acid (GCA) added into hydrogen peroxide (H2O2) or urea-hydrogen peroxide (U-H2O2) slurries on Cu-CMP performance were investigated. Experiments showed that GCA could prevent H2O2 or U-H2O2from rapid decomposition and increase the active peroxide lifetime of the slurries. In addition, electrochemical studies from polarization and impedance experiments verified that copper removal efficiency could be enhanced by use of GCA. Meanwhile, a valid equivalent circuit for Cu-CMP system was proposed, and the fitting results provided a good index to surface planarization. Furthermore, GCA could shorten the range of isoelectric points between Cu film and a-Al2O3abrasives. After a post cleaning, the particle contamination thus could be reduced due to the elec-trostatic repulsion. Our study proved that adding GCA into the U-H2O2slurries with BTA could further improve the Cu-CMP performance.
2004 Elsevier B.V. All rights reserved.
Keywords: Glycolic acid; Urea-hydrogen peroxide; Slurry; Copper; Chemical mechanical polishing
1. Introduction
Chemical mechanical polishing (CMP) of metal is widely recognized as the key technique to obtain global planarization for copper multilevel
inter-connection in IC manufacturing [1]. However,
the planarization mechanisms of metal CMP in-volve complicated chemical reactions and physical actions. So it is difficult to control the CMP per-formance, especially for a high corrosion-sensitiv-ity metal like Cu. According to different slurry components, the planarization mechanisms of me-tal CMP can be summarized as the following two types. The first one is that the metal surface may be polished with a dissolution-type slurry in which no surface film forms. In this case, the CMP
0167-9317/$ - see front matter 2004 Elsevier B.V. All rights reserved. doi:10.1016/j.mee.2004.10.008
*
Corresponding author. Tel.: +886228927154x8041; fax: +886228960255.
E-mail address:[email protected](T.-H. Tsai).
process proceeds by the mechanical removal and chemical dissolution of metal itself[2]. In the sec-ond type of mechanisms, a thin abradable layer is continuously formed on metal surface by the reactions of metal and slurry components. These slurry components may include oxidants, inhibi-tors and other film-forming agents. The thin abradable layer is then scanned away rapidly by the mechanical action or dissolves in the slurry with a chelating agent. Once the mechanical pol-ishing process has stopped, a thin passive film re-mains on the surface and inhibits the proceeding
of wet etching [3]. Therefore, controlling CMP
process to reach global planarization is much eas-ier due to this mechanism.
The chemical components and properties of slurry determine the Cu-CMP performance princi-pally. As a result, many studies devoted to the development of copper slurries with high planari-zation ability and CMP efficiency. According to the second mechanism mentioned above, oxidants with high oxidizing ability and low contamination should be required to form a passive film on Cu
surface. Hydrogen peroxide (H2O2) is a widely
used example at present [4,5]. However, H2O2
decomposes to H2O and O2easily, and this
decom-position will result in the slurry transport issues, unstable CMP performance and short shelf
life-time. Recently, urea-hydrogen peroxide
(U-H2O2) has been proposed as the oxidant for
Cu-CMP slurries due to its less self-decomposition
and better oxidizing performance during CMP[6].
Also, Kaufman and Kistler[7]reported that
or-ganic acids can be added into metal slurries to en-hance CMP performance by acting as pH adjusters or chelating agents. On the other hand, many researchers have examined the further efficiency of organic acids, and it was found that the action of organic acids would depend on the different CMP conditions. For instance, in 1999, Hu et al.
[8]indicated that citric acid can inhibit Cu
corro-sion in HNO3slurries, and Zhang et al.[9]found
that citric acid can prevent the alumina-particle deposition on tungsten surface. Even though many organic acids, such as acetic acid [10], oxalic acid
[11], ethylenediamine tetraacetic acid (EDTA)
[12] and amino acid[13,14]have been extensively
studied, glycolic acid (GCA) has never been used.
As known, GCA is easy handling, water-soluble, biodegradable, non-volatile and can efficiently che-late the metal. Therefore, the objective of this pa-per is to investigate the effect of GCA added into
U-H2O2 slurries on electrochemical behaviors of
Cu CMP. In addition to the measurement of polarization curves, the electrochemical impedance spectroscopy (EIS) was also obtained, and the equivalent circuit of surface reactions during Cu CMP was proposed. Although the equivalent cir-cuits of Al have been discussed[15], fewer studies examined that in Cu CMP. In this study, the spe-cific role of GCA and the information of the
equiv-alent circuit for CMP in U-H2O2-based slurries
were explored. Our experiments proved that GCA could improve Cu-CMP efficiency, and the planarization mechanisms of Cu CMP could be described well by the electrochemical methods.
2. Experimental
Commercial pure Cu sheets with 0.3-mm thick-ness were used, and the dimension of each
speci-men was 1· 1 cm2 for electrochemical
measuring. In addition, 3-in. wafers with an elec-troplated Cu film were polished to obtain removal rates and surface roughness. All specimens were degreased by the cathode electrochemical method at 6 V for 20 s, and then were cleaned in 3 wt%
H2SO4solution followed by deionized (DI) water
rinsing. Afterward, the samples were dried in nitrogen gas and transferred to the electrochemical measuring equipment or polishing machine. The slurry was prepared by use of 50-nm alumina par-ticles (a-Al2O3), and its solid concentration in the
slurry was fixed at 5 wt% for all of the experi-ments. To investigate the effects of different chem-ical components on Cu CMP, we prepared the slurries by analytical grade reagents, including
urea-hydrogen peroxide (U-H2O2), benzotriazole
(BTA) and glycolic acid (GCA).
For the purpose to compare the stability of solutions, 5 wt% U-H2O2and 1.8 wt% H2O2, with
the equal level of peroxide in solutions, were peri-odically analyzed by titration with 1 wt% potas-sium permanganate solution to determine the peroxide activity. An acoustic spectrometer, model
DT-1200, was used to determine the zeta poten-tials of materials in different pH values adjusted
by HNO3 or NH4OH. Dipping experiments were
conducted to determine the particle contamination on Cu surface. For dipping experiments, 300-nm
a-Al2O3 particles were used in slurries for SEM
observation. After dipped in slurries for 30 s, Cu samples were rinsed gently with DI water prior to SEM study.
The electrochemical test-cell was composed of Cu working electrode, platinum counter electrode and Ag/AgCl reference electrode, with a Luggin probe. The downward pressure and the rotating speeds during abrasion were 5 psi and 100 rpm, respectively. The dc electrochemical experiments were conducted by use of a potentiostat of EG&G, model 273A, while the corrosion software of EG&G, model 352, was adopted for electro-chemical calculations. The dc polarization curves with a voltage scan rate of 5 mV/s were selected to measure the corrosion current densities and po-tential. Meanwhile, the corrosion current density was converted to the corresponding corrosion rate (CR) in nm/min according to FaradayÕs law. In addition, EIS measuring was performed with an electrochemical interface system of Solartron, FRA 1260 and 1286, and a small amplitude per-turbation of 10 mV in a sinusoidal wave was
ap-plied with the operated frequency, 105–102 Hz,
to ensure the linearity for impedance analysis. For polishing experiments, a Lapmaster LM-51 polisher, operated at 80 rpm/60 rpm of the platen/
carrier rotating speeds, was used with the polishing pad of IC 1000/SUBA IV supplied by Rodel. Be-fore CMP, the slurry had to be stirred in a mixer to maintain the slurry suspension for the test per-iod. During CMP, the slurry was delivered to the gap between Cu and the pad with a flow rate of 100 ml/min. The removal rate (RR) was calculated from the weight loss of Cu sheets before and after 5-min polishing, and the results were obtained by the average of three tests. Before or after CMP, the surface morphology of specimens was charac-terized by an atomic force microscope (AFM), and the surface rms-roughness (Rq) was calculated
by the software package.
3. Results and discussion 3.1. Durability of slurries
As mentioned above, the oxidant acts an impor-tant role of film-formation in CMP slurry. In this
study, we chose two peroxides, H2O2 and
U-H2O2, as the oxidants. Table 1 lists the active
percentages of H2O2and U-H2O2, relative to their
initial values, and the pH values in various hydro-gen peroxide-based solutions. The results indicated that the active peroxide percentage in 1.8 wt% H2O2solution degraded at a faster rate than that
in 5 wt% U-H2O2 solution, but their pH values
were similar. Additionally, the degradation rates of the active peroxide percentage showed large
Table 1
Changes of active peroxide percentage (%) and pH value with time in various H2O2or U-H2O2slurries
Time (h) 0 10 50 100 250 500 1.8 wt% H2O2 % 100.0 96.35 75.16 57.42 41.99 33.44 pH 5.56 5.52 5.31 5.45 5.03 5.18 1.8 wt% H2O2+ 1 wt% NH4OH % 100.0 23.75 20.12 18.15 16.41 15.08 pH 10.03 10.21 9.78 9.65 9.41 9.32 1.8 wt% H2O2+ 1 wt% GCA % 100.0 96.01 83.24 71.31 64.02 57.88 pH 1.98 2.03 2.07 2.13 2.02 2.21 5 wt% U-H2O2 % 100.0 98.52 93.02 91.04 89.75 87.48 pH 5.87 5.65 5.89 5.76 5.81 5.92 5 wt% U-H2O2+ 1 wt% NH4OH % 100.0 76.12 52.43 48.21 35.02 31.80 pH 10.62 10.58 10.64 10.47 10.32 10.20 5 wt% U-H2O2+ 1 wt% GCA % 100.0 97.82 96.01 94.23 93.31 91.59 pH 2.04 2.10 2.08 2.11 1.94 2.07
variations when the U-H2O2 or H2O2-based
solutions were mixed with NH4OH or GCA. In
Cu-CMP slurry, NH4OH has been a well-known
chelating agent. However, it was found the active
peroxide percentage of 5 wt% H2O2solution with
1 wt% NH4OH reduced to 23.75% of its initial
value after only 10 h. Even though H2O2was
re-placed by U-H2O2, the peroxide activity of 5
wt% U-H2O2solution with 1 wt% NH4OH also
re-duced to 31.8% after 500 h. On the contrary, the addition of GCA, another chelating agent for Cu, could enhance the durability of slurries. After 500 h, the active peroxide percentage still exhibited a high level, 91.59%, for the 5 wt% U-H2O2
solu-tion with 1 wt% GCA. Also, the 5 wt% H2O2
solu-tion with 1 wt% GCA had higher peroxide activity
than that with NH4OH. This showed that using
GCA as a chelating agent instead of NH4OH
could form a stable solution with a longer shelf lifetime for hydrogen peroxide-based CMP slurry. 3.2. Polarization curves
The abrasion effect on the polarization curves
of Cu in various slurries are shown in Fig. 1and
Fig. 2, and their corresponding corrosion parame-ters and Cu removal rates (RR) are all listed in
Table 2. The first thing noticeable is the difference
between polarization curves of Fig. 1, especially
the corrosion potential drop after abrasion
(DEd). It is obvious that DEdin 1 wt% GCA slurry
was smaller than that in 5 wt% U-H2O2. As
re-ported [16], the potential drop is attributed to
the change on sample surface from the formation of passive film to its removal. Therefore, as shown in Fig. 1, the larger DEd in 5 wt% U-H2O2
illus-trated a faster formation and a quicker removal of the passive film on Cu surface. On the other hand, Cu in 1 wt% GCA with a higher anodic cur-rent density, relative to 5 wt% U-H2O2, exhibited a
faster dissolution rate of Cu due to the chelating action between Cu surface and GCA. In further comparison with the corrosion parameters in
Table 2, the corrosion potential and corrosion
cur-rent density were both higher in 5 wt% U-H2O2
than those in 1 wt% GCA. This was attributed to the Cu with higher oxidation state and greater oxidizing rate in U-H2O2 solution. Thus, it could
be shown again that U-H2O2owned a strong
oxi-dizing action for Cu, and the formed passive film could protect Cu from deeper corrosion.
When 5 wt% U-H2O2 was mixed with 1 wt%
GCA, DEd decreased drastically but the anodic
current density of Cu increased as shown in
10-7 1x10-5 10-3 -400 -200 0 200 400 600 1 w% GCA 5 w% U-H2O2 no abrasion abrasion E (mV vs Ag/AgCl ) i (A/cm2)
Fig. 2. It resulted from the thinning passive film on Cu surface by the chelating action of GCA, so the Cu consumption was enhanced by both chelating and polishing. Thus, as listed inTable 2, the high corrosion rate, 19.59 nm/min, and removal rate, 605.82 nm/min, were obtained in the mixed slurry,
5 wt% U-H2O2 and 1 wt% GCA. Furthermore,
Fig. 2also shows that DEdincreased substantially
by adding 0.1 wt% BTA into 5 wt% U-H2O2and 1
wt% GCA slurry even though the current density still maintained a low level. It indicates that Cu
in 5 wt% U-H2O2 slurry with 1 wt% GCA and
0.1 wt% BTA showed the high mechanical sensitiv-ity and good anti-corrosion capabilsensitiv-ity. As a result, the Cu removal rate attained 594.14 nm/min, but
the corrosion rate reduced to 3.37 nm/min in this mixed slurry. The AFM micrographs of Cu sur-face before and after CMP with this slurry are
shown in Fig. 3(a) and (b), respectively. In
com-parison with the AFM images, it shows the surface roughness could be reduced efficiently after CMP
with the proposed slurry, 5 wt% U-H2O2, 1 wt%
GCA and 0.1 wt% BTA. 3.3. EIS results
The EIS results of Cu in the slurry of 5 wt%
U-H2O2, 1 wt% GCA and 0.1 wt% BTA are
pre-sented by Nyquist and Bode plots as shown in
Fig. 4(a) and (b), respectively. When Cu was
10-7 1x10-5 10-3 0 300 600 with 0.1 w% BTA 5 w% U-H 2O2 + 1 w% GCA no abrasion abrasion E (mV vs Ag/AgCl ) i (A/cm )2
Fig. 2. Effects of abrasion and BTA on polarization curves for Cu in 5 wt% U-H2O2with 1 wt% GCA slurries (abrasion: 5 psi and 100 rpm).
Table 2
Summary of corrosion parameters and removal rates (RR) of Cu in various slurries
Slurry No abrasion Abrasion DEda(mV) RR (nm/min) CR (nm/min)
Ecorr(mV) icorr(A/cm2) Ecorr(mV) icorr(A/cm2)
5 wt% U-H2O2 153 1.13· 104 46 1.33· 104 107 472.63 2.92 1 wt% GCA 8 1.42· 105 3 4.48· 105 11 184.30 1.07 5 wt% U-H2O2+ 1 wt% GCA 182 4.60· 104 145 8.85· 104 37 605.82 19.59 5 wt% U-H2O2+ 1 wt% GCA + 0.1 wt% BTA 323 9.63· 105 191 1.53· 104 132 594.14 3.37 a DE
immersed in the mixed slurry, a dual non-ideal semicircle response of Nyquist plot, shown in
Fig. 4(a), could be found. As Griffin et al. [17]
pointed out, this response is caused from the for-mation of the secondary conduction paths or dis-continuities within the copper oxide layer at or near the incoherent precipitates. Thus, the con-stant-phase-element (CPE) was adopted in the equivalent circuit to fit the behaviors at the inter-face of Cu and slurry[6]. Furthermore, it has been reported the inductor response in the low fre-quency range is due to the adsorption or the
evo-lution of gas on surface [18]. Therefore, our
equivalent circuit for describing Cu CMP would also contain the inductor element. In summary of the above facts, the electrochemical reactions at the interface of Cu and slurry would be simulated by the equivalent circuit ofFig. 5. As shown in this figure, the equivalent circuit consists of solution
resistance (Rs), double-layer CPE (CPEdl),
charge-transfer resistance (Rct), passive-film CPE
(CPEpf), passive-film resistance (Rpf) and
adsorp-tion inductance (Lad). The fitting results by use
of CPEs, presented by the solid lines inFig. 4(a) and (b), would approach those experiment results rather than those by use of capacitors.
The results are also displayed by the Bode plot in Fig. 4(b). According to ac impedance theory
[18], the impedance at frequency A and B,
indi-cated by the dashed lines of Fig. 4(b), can be
re-garded as Rs+ Rpf+ Rct, and Rs+ Rpf,
respectively, and the impedance at sufficiently high frequency, 105Hz, is Rs. Thus, we could calculate
these resistances from the Bode plot. It was found
that Rsapproached 78.88 X cm2when Cu was
im-mersed into the mixed slurry, 5 wt% U-H2O2, 1
wt% GCA and 0.1 wt% BTA. The polishing, how-ever, increased Rsto 87.28 X cm2due to the
smal-ler fluid pathway between Cu surface and the pad. In addition, rise in Rpfand Rctcould be found with
the increasing immersion time. The result indi-cated that the adsorbed BTA-layer and the formed oxide film inhibited the reactions continuously, and this caused the resistance to increase. As a
Fig. 3. AFM micrographs of Cu surface with roughness (Rq): (a) before CMP, and (b) after CMP with the mixed slurry, 5 wt% U-H2O2, 1 wt% GCA and 0.1 wt% BTA.
mechanical action of 5 psi and 100 rpm was ap-plied, the adsorbed layers and passive films were
destroyed, and then Rpf and Rct reduced
substantially.
Moreover, the phase angle in Fig. 4(b) also
shows that the high-frequency peak was related to the passivation while the low-frequency peak was affected by the surface reactivity. The former was lowered in most of the CMP duration, and the latter was raised with the increasing immersion time. Also, the positive phase-angle value, depend-ing on the adsorption, increased with the immer-sion time and disappeared during CMP. All of
the above results indicated that the formation of gas, the adsorption of BTA-layer and the genera-tion of oxide film on the Cu surface could be illus-trated well by the proposed equivalent circuit, and also the behaviors sensitive to the mechanical force could be investigated.
3.4. Relationship between CPE and surface roughness
In our observations, the passive film on Cu sur-face was a loose oxide layer, and its sursur-face was of-ten rough and porous. So a non-ideal capacitor
10-1 100 101 102 103 104 105 5 0 -5 -10 -15 -20 B A 5 w% U-H 2O2 + 1 w% GCA + 0.1 w% BTA 1 min immersion 3 min immersion 6 min immersion during CMP
Phase Angle (degree)
Frequency (Hz) 80 100 200 400 600 800 1000 Impedance ( Ω -cm ) 2 100 200 300 400 0 -100 -200 -300 increasing ω Z''( Ω -cm 2) Z'(Ω-cm )2
5 w% U-H2O2 + 1 w% GCA + 0.1 w% BTA
1 min immersion 3 min immersion 6 min immersion during CMP (a) (b)
Fig. 4. Effects of immersion time and CMP on: (a) Nyquist plot and (b) Bode plot for Cu in 5 wt% U-H2O2, 1 wt% GCA and 0.1 wt% BTA slurry. Simulated results are represented by the solid curves (CMP: 5 psi and 100 rpm).
was induced into the equivalent circuit for simulat-ing the interface behaviors of Cu and slurry. The CPE herein was substituted for the ideal capacitor.
The CPE impedance is written as[19],
ZCPE ¼ ½T ðjxÞn1;
where T is a general admittance function, j is the complex operator ðpffiffiffiffiffiffiffi1Þ, and n is an adjustable parameter that usually lies between 0.5 and 1. When n = 1, the CPE describes an ideal capaci-tance with the high planarization or
homogene-ities. For the case of n = 0.5, a Warburg
impedance relation is obtained; this impedance is associated with the concentration and the diffu-sion-related processes. Generally, the deviation from the ideal surface film, i.e. ideal capacitor, can be estimated by this adjustable parameter.
Fig. 6, containing the Cu-CMP results by use of U-H2O2-based slurries in Ref. [6], illustrates the
dependence between the adjustable parameters and the roughness. In which, the parameters such as double-layer (ndl) and passive film (npf) were
in-cluded, and the roughness (Rq) was calculated by
the AFM technique. Obviously, it exhibited that all of the npfvalues were lower than the ndlvalues
and independent of the roughness. On the con-trary, ndlseemed further relevant to the Cu surface
roughness (Rq). The reason was evident that CPEpf
was involved in the porous passive layer while CPEdlwas affected only by the Cu surface. As a
re-sult, the ndl value could provide a good index to
monitor the planarization-performance on Cu surface. It was also found inFig. 6that the lowest surface roughness, 2.64 nm, was obtained in the
U-H2O2slurry mixed with 0.1 wt% BTA and 1 wt%
NH4OH instead of GCA. Even though the slurry
containing GCA was not the best choice for pla-narity, the addition of GCA still could enhance the slurry stability. As reported[20], a stable slurry is important for good CMP performance because it can not only improve CMP reliability but also reduce the defects of the surface after CMP. 3.5. Surface potential and particle contamination
Fig. 7 shows the zeta potentials of Cu and
a-Al2O3 particles as a function of pH in 0.1 wt%
BTA solutions with or without 1 wt% GCA. The corresponding isoelectric points (IEPs), the pH of
zero charge, of Cu and a-Al2O3without GCA were
0.725 and 9.109, respectively. This meant that the Cu and a-Al2O3surfaces had opposite charges for
pH values from 0.725 to 9.109. The opposite charges resulted in the attraction, and then
a-Al2O3 particles would be easily deposited on Cu
surface and difficultly removed. However, when 1 wt% GCA was added to the solutions, the IEPs of Cu and a-Al2O3reduced to 3.672 and 6.253,
respec-tively. Obviously, the pH range of Cu and a-Al2O3
with opposite charges was shortened as shown in
Fig. 7. This indicates that a-Al2O3deposition could
be inhibited by use of GCA due to the electrostatic
0 2 4 6 8 10 12 -60 -40 -20 0 20 40 60 Zeta Potential (mV) pH α -Al2O3 Cu 1 w% GCA α -Al2O3 Cu
Fig. 7. Zeta potentials of a-Al2O3and Cu as a function of pH in 0.1 wt% BTA solutions with or without 1 wt% GCA.
0.6 0.8 1.0 0 2 4 6 8 Roughness (nm) n npf ndl 5 w% U-H2O2 5 w% U-H2O2 + 0.1 w% BTA 5 w% U-H2O2 + 0.1 w% BTA + 1 w% NH4OH 5 w% U-H2O2 + 0.1 w% BTA + 1 w% GCA
Fig. 6. Surface roughness vs. the adjusted parameters of passive film, npf(filled symbol) and double layer capacitances, ndl(hollow symbol) in various slurries for Cu CMP at 5 psi and 100 rpm.
repulsion. Fig. 8 displays the SEM images of a-Al2O3contamination, shown by those white points,
on Cu surface. It shows that a clearer Cu surface, with less a-Al2O3deposition, was obtained by use
of the slurry with 1 wt% GCA. These SEM images supported the above results of zeta potential.
4. Conclusions
In this study, the effect of glycolic acid (GCA) on Cu CMP was investigated by electrochemical methods, including titration, polarization and impedance experiments. The results showed that GCA could increase the stability of slurries by
pre-venting the hydrogen-peroxide component from rapid decomposition. The electrochemical studies from polarization and impedance measurements verified that GCA could chelate with Cu and cop-per oxide on the polished surface in the existence of oxidants and inhibitors. Thus, the Cu-CMP per-formance could be enhanced by use of GCA, and the Cu removal rate could achieve 594.14 nm/min with a low surface roughness, 6.09 nm, in the mixed
slurry, 5 wt% U-H2O2, 1 wt% GCA and 0.1 wt%
BTA. In addition, a deliberate equivalent circuit for Cu-CMP system was proposed. The fitting re-sults of EIS showed that the adjustable parameter of double-layer CPE (ndl) would depend on the
sur-face roughness and could be regarded as an index
Fig. 8. SEM images of Cu samples dipped for 30 s in 5 wt% a-Al2O3(300 nm) and 0.1 wt% BTA slurries: (a) without GCA; (b) with 1 wt% GCA.
to CMP planarization. The slurry with GCA still could result in the electrostatic repulsion between
Cu surface and a-Al2O3 over a pH range larger
than that without GCA. Therefore, the addition of GCA into copper slurries could efficiently de-crease particle contamination and easily enhance the post-CMP cleaning process.
Acknowledgements
The authors would like to thank the National Science Council in Taiwan for financially support-ing this research under Contract No. NSC 93-2214-E-149-001. Also, the authors are pleased to acknowledge the help extended by Northern Taiwan Institute of Science and Technology and National Taiwan University.
References
[1] H. Xiao, Introduction to Semiconductor Manufacturing Technology, Prentice-Hall, Inc., New Jersey, 2001. [2] J.M. Steigerwald, R. Zirpoli, S.P. Murarka, D. Price, R.J.
Gutmann, J. Electrochem. Soc. 141 (1994) 2842. [3] F.B. Kaufman, D.B. Thompson, R.E. Broadie, M.A. Jaso,
W.L. Guthrie, D.J. Pearson, M.B. Small, J. Electrochem. Soc. 138 (1991) 3460.
[4] M. Ziomek-Moroz, A. Miller, J. Hawk, K. Cadien, D.Y. Li, Wear 255 (2003) 869.
[5] T. Du, Y. Luo, V. Desai, Microelectron. Eng. 71 (2004) 90.
[6] T.H. Tsai, Y.F. Wu, S.C. Yen, Appl. Surf. Sci. 214 (2003) 120.
[7] V.B. Kaufman, R.C. Kistler, US Pat. 5,954,997, 1999. [8] T.C. Hu, S.Y. Chiu, B.T. Dai, M.S. Tsai, I.C. Tung, M.S.
Feng, Mater. Chem. Phys. 61 (1999) 169.
[9] L. Zhang, S. Raghavan, S. Meikle, G. Hudson, J. Electrochem. Soc. 146 (1999) 1442.
[10] J.M. Steigerwald, S.P. Murarka, R.J. Gutmann, D.J. Duquette, Mater. Chem. Phys. 41 (1995) 217.
[11] K. Yang, S. Avanzino, C.M.C. Woo, US Pat. 6,143,656, 2000.
[12] S. Aksu, F.M. Doyle, J. Electrochem. Soc. 149 (2002) B340.
[13] M. Hariharaputhiran, J. Zhang, S. Ramarajan, J.J. Kele-her, Yuzhuo Li, S.V. Babu, J. Electrochem. Soc. 147 (2000) 3820.
[14] S. Aksu, F.M. Doyle, J. Electrochem. Soc. 149 (2002) B352.
[15] H.S. Kuo, W.T. Tsai, J. Electrochem. Soc. 147 (2000) 149.
[16] T.H. Tsai, S.C. Yen, Appl. Surf. Sci. 201 (2003) 190. [17] A.J. Griffin, F.R. Brotzen, C.F. Dunn, J. Electrochem.
Soc. 141 (1994) 3473.
[18] J.R. Macdonald, Impedance Spectroscopy, Wiley, New York, 1987.
[19] R. Babic, M.M. Hukovic, A. Jukic, J. Electrochem. Soc. 148 (2001) B146.
[20] L. Zhang, S. Raghavan, M. Weling, J. Vacuum, Soc. Technol. B 17 (1999) 2248.