MEGASONIC CLEANING OF WAFERS IN ELECTROLYTE SOLUTIONS: POSSIBLE ROLE OF ELECTRO-ACOUSTIC AND CAVITATION EFFECTS. The University of Arizona, Tucson

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MEGASONIC CLEANING OF WAFERS IN ELECTROLYTE SOLUTIONS: POSSIBLE ROLE OF ELECTRO-ACOUSTIC AND CAVITATION EFFECTS Manish Keswani 1, Srini Raghavan 1, Pierre Deymier 1 and Steven Verhaverbeke 2 1 The University of Arizona, Tucson 2 Applied Materials 1

Outline INTRODUCTION PROPOSED WORK EXPERIMENTAL MATERIALS AND METHODS RESULTS AND DISCUSSION SUMMARY FUTURE WORK 2

INTRODUCTION 3

Growth and Challenges Integrated Circuit Industry Fifty Percent of yield losses due to particle contamination Over 200 cleaning steps Critical particle diameter and count to be 25 nm and 59 #/wafer respectively for a 300 mm wafer Particulate impurities on the wafer critically affects the device performance, reliability, and product yield of integrated circuits ITRS Requirements 4

Typical Wafer Cleaning Sequence 120-150 deg C 10 min 25 deg C 25 deg C 1 min 25 deg C H 2 SO 4 :H 2 O 2 4:1 to 2:1 DI Water Rinse HF:H 2 O 1:50 to 1:100 DI Water Rinse 80 deg C 10 min SC-2 HCl:H 2 O 1:5 to 1:200 DI Water Rinse SC-1 NH 4 OH:H 2 O 2 :H 2 O 1:1:5 to 1:1:200 DI Water Rinse 25 deg C 25 deg C 80 deg C 10 min 5

Etching of Thermal Oxide in SC1 (time = 1 min) Oxide Etched (Å) 1 0.8 0.6 0.4 1:1:50 1:1:125 1:1:200 0.2 0 20 25 30 35 40 45 50 55 60 Temperature (deg C) Strong Etch Dependence on Temp Courtesy: Dr. J. Butterbaugh, FSI 6

Wafer Cleaning Techniques High Pressure Water Jet Cleaning Immersion Cleaning and Spray Cleaning without Megasonics Immersion Cleaning and Spray Cleaning with Megasonics Very simple and easy to use. Great potential in removing sub micron size particles in combination with dilute chemistries 7

Megasonic Cleaning MHz frequency sound waves with different cleaning chemistries Particle on wafer surface Hydrodynamic boundary layer thickness 400-1000 µm in DI water (viscosity = 10-3 Pa-s, density = 10 3 kg/m 3, velocity = 0-10 m/s ) Acoustic boundary layer at 1 MHz in DI water ~ 0.5 µm Particle Removal Mechanisms: Acoustic Streaming: Drag forces and rolling moments @S/L interface to help particle removal. Acoustic Cavitation: High energy shock waves or fluid jet dislodging the particle. Chemistry + Sonic field 8

Physical Effect of Cavitation Sonoluminescence (Photon emission ) At collapse, the gas inside the cavity reaches extremely high temperatures (4300 K) and pressures (few hundred bars). Results in production of free radical species (excited hydroxyl radicals). Recombination of free radicals gives rise to photon emission. 3 H O + M H O ( B ) + M 2 2 * 1 3 1 H 2O* ( B1 ) + M H 2O( A1 ) + hν 0 (270 290 nm) 3 H 2O* ( B1 ) + M H + OH * OH + H + hν 1 (310nm) 9

Challenges Associated with Megasonic Cleaning Megasonic cleaning is typically done in alkaline ph condition (using SC1-1 solution) which causes loss of wafer surface due to etching Use of DI water instead of SC-1 requires much higher power density. A significant level of damage of features (in the case of patterned wafers) occurs at these power densities # Defects/mm 2 for 30nm Si line defects/mm 2 300 250 200 150 100 DIW dilute SC1(1:1:100)@RT dilute NH4OH(1:100)@RT 76.92 192.3 153.84 269.23 230.76 192.3 50 0 19.23 0 0 0.5 1 1.5 2 2.5 Power (W/cm 2 ) Images from -H. Shende, MS Thesis, The University of Arizona, 2006 10

PROPOSED WORK 11

Need for Present Work 1) Identify a non-etching chemistry with advanced non-damaging megasonics 2) Focus of Past Work Acoustic Power Chemistry Gas content Surface tension Viscosity No literature on effect of Ionic Strength on Particle Removal Studies in Megasonics Industry uses cleaning solutions (eg SC1, SC2, TMAH, Piranha etc) which may have varying ionic strengths Use of Electrolytes can achieve both objectives 12

Density (Kg/m 3 ) Why Study KCl Solutions? Addition of KCl to water increases the bulk modulus (κ) and density (ρ 0 ) of solution and hence may modulate the pressure amplitude (a) of the propagating sound wave and affect Cavitation The propagation of sound waves through an electrolyte solution containing particles is known to result in the generation of two types of oscillating electric potentials, namely, Ionic Vibration Potential (IVP) and Colloid Vibration Potential (CVP). These potentials and their associated electric fields can exert forces on particles adhered to a surface, resulting in their removal. 0.5 a = 2 I ρ κ 0. 1025 1020 1015 1010 1005 1000 2.38E+09 2.36E+09 2.34E+09 2.32E+09 2.30E+09 2.28E+09 2.26E+09 2.24E+09 BulK Modulus (kg/m-sec 2 ) Pressure Amplitude (atm) 2.61 2.6 2.59 2.58 2.57 2.56 2.55 ( ) ( ) 25 0 I = Intensity of transducer=2.17 W/cm 2 995 0 0.1 0.2 0.3 0.4 0.5 0.6 KCl Concentration (M) 2.22E+09 2.54 0 0.1 0.2 0.3 0.4 0.5 0.6 KCl concentration (M) 13

Debye Effect S. D. Vidal et al., J. Phy. Chem., 99, pp.6733-6738 (1995) 14

Interaction of Sonic Field with Colloidal Particles: Colloid Vibration Potential (CVP) periodic polarization of the ionic atmosphere surrounding the particles. Acoustic Field CVP ~ 5 to 10 mv for silica suspensions subjected to sound waves of 0.2 MHz at 0.22 W/cm 2 of power density periodic polarization causes each particle to act as a vibrating dipole E. Yeager et al.,, The Journal of the Acoustical Society of America, 25, 3, 456-460 (1953) 15

Dipole Moment Formation Due to Asymmetry of Double Layer Around a Charged Particle Adhered on a Wafer Surface Bulk Phase Bulk Phase Acoustic Field Wafer Surface Bulk Phase Bulk Phase Can the electric field associated with CVP exert a force on charged particles adhered to a surface, resulting in their removal? 16

EXPERIMENTAL MATERIALS AND METHODS 17

Hydrophone-Oscilloscope Experiments Method and Analysis Experiments were performed in a Prosys immersion megasonic system using a hydrophone (Onda Corporation/Specialty Engineering) which was positioned in the far field region to achieve consistency in results. The set up has a capacity to acquire 65000 continuous samples for each run. Sampling rate was 20 million samples/sec. The output signal, in volts, from the oscilloscope is then converted to the Root Mean Square value. Fast Fourier Transform of the raw output signal was performed to convert the data from time to frequency domain. 2.5 inch Oscilloscope 1.5 mm Hydrophone Hydrophone donated by Dr. Steven Verhaverbeke, Applied Materials 18

Spectral Analysis using Fast Fourier Transform ρ ω r2 R r2 = 3 γ (P 0 +2σ/R r ) - 2 σ/r r ρ is the density of the liquid ω r is the resonance frequency of the bubble R r is the radius of the resonating bubble γ is the ratio of specific heats of the gas P 0 is the steady pressure in the absence of the sound field σ is the surface tension of liquid Radius of bubble (micron) Relative Bubble Number 19

How to measure cavitation??? Donated by Mark Beck Prosys Megasonics Detects Sonoluminescence produced by Cavitation (Spectral Range 270-650 nm) Real Time Monitoring of Cavitation Density Indicator of Feature Damage 20

Wafer Pre-clean, Contamination and Cleaning Protocol Pre-cleaning of 150-mm silicon wafers in 1:1:50 SC1 solution Aminated and Plain silica particles (Mean Size ~ 370 ± 20 nm purchased from Corpuscular Inc.) used for contamination. Typical particle count on wafers after deposition : 2500 Cleaning done in a Prosys immersion megasonic tank for one minute at 30 0 C Surfscan 5500 used for particle counts 21

RESULTS AND DISCUSSION 22

Role of KCl on Sound Wave Amplitude Root Mean Square (V) 0.07 0.06 0.05 0.04 0.03 0.02 0.01 DI KCl soln ( ~ 0.019 M) Root Mean Square (V) 0.07 0.06 0.05 0.04 0.03 0.02 0.01 DI KCl soln ( ~ 0.096 M) 0 0 0.5 1 1.5 2 2.5 Megasonic Power (W / cm2) 0.07 DI KCl soln ( ~ 0.3 M) T = 33 C 0 0 0.5 1 1.5 2 2.5 Megasonic Power (W / cm2) 0.07 DI KCl soln ( ~ 0.5 M) Root Mean Square (V) 0.06 0.05 0.04 0.03 0.02 0.01 0 0 0.5 1 1.5 2 2.5 Megasonic Power (W / cm2) Root Mean Square (V) 0.06 0.05 0.04 0.03 0.02 0.01 0.00 0 0.5 1 1.5 2 2.5 Megasonic Power (W / cm2) 23

Cavity Size Distribution from FFT and Energy Balance Correlating frequencies of oscillating bubbles with their sizes Relative number of bubbles 1000 100 10 KCl Concentration = 0.02 M, Power Density = 2.17 W/cm 2 1 1.E-07 1.E-06 1.E-05 1.E-04 1.E-03 Increasing appearance of bubbles with increase In KCl concentration Distribution of bubbles between 1-1000 micron Bubble size larger than about 1 mm can be ignored as such bubbles will be removed from the system due to buoyancy. Radius of gas bubble (m) 1000 KCl Concentration = 0.1 M, Power Density = 2.17 W/cm 2 ) 1000 KCl concentration = 0.5 M, Power density = 2.17 W/cm 2 Relative number of bubbles 100 10 Relative number of bubbles 100 10 1 1.E-07 1.E-06 1.E-05 1.E-04 1.E-03 Radius of gas bubble (m) 1 1.E-07 1.E-06 1.E-05 1.E-04 1.E-03 Radius of gas bubble (m) 24

Sonoluminescence in KCl Solution Frequency (#) 1600 1400 1200 1000 800 600 2.17 W/cm2 DI 2.17 W/cm2 KCl 0.6 M 2.17 W/cm2 KCl 1.1 M T = 30 0 C 400 200 0 1.E+05 1.E+06 1.E+07 Counts/sec 25

Zeta Potential of Aminated and Plain Silica Particles Aminated silica Plain silica 80 60 Ionic Strength = 0.01 M Zeta Potential (mv) 40 20 0-20 -40 3 3.5 4 4.5 5 5.5 6 6.5 7 7.5 8 8.5 9-60 -80 ph The isoelectric point (IEP) of aminated silica and plain silica particles was found to occur at ph values of 7.1 and 3.9 respectively. 26

Megasonic Removal of Plain Silica Particles in KCl Solutions of Different Concentration KCl soln DI only KCl at 0 W 100 80 60 ph = 6.0 T = 30 0 C Power Density = 0.077 W/cm 2 PRE % 40 20 0 1.00E-08 1.00E-07 1.00E-06 1.00E-05 1.00E-04 1.00E-03 1.00E-02 1.00E-01 1.00E+00 1.00E+01-20 Ionic Strength (M) 27

Megasonic Removal of Plain Silica Particles in 0.57 M KCl Solution at Different Power Densities DI 0.57 M KCl 100 90 ph = 6.0 PRE % 80 70 60 50 40 30 20 10 0 0.04 0.05 0.06 0.07 0.08 0.09 0.1 Power Density (W/cm 2 ) T = 30 0 C 28

Megasonic Removal of Aminated Silica Particles in KCl Solutions of Different Concentration at Different Power Densities 100 80 Aminated silica ( KCl) (0.43 W/cm2) Aminated Silica (DI only) (0.43 W/cm2) Plain silica (KCl) (0.077 W/cm2) Plain silica (DI only) (0.077 W/cm2) Aminated silica (1 M) ( 0 W ) Aminated silica(kcl) (0.077 W/cm2) Aminated silica (KCl) (0.22 W/cm2) Aminated silica (0.1 M) ( 0 W ) Plain silica (DI only) (0.11 W/cm2) Aminated silica(kcl) (0.129 W/cm2) Aminated silica(kcl) (0.103 W/cm2) Aminated silica(kcl) (0.09 W/cm2) T = 30 0 C 60 P R E % 40 20 0 1.E-08 1.E-07 1.E-06 1.E-05 1.E-04 1.E-03 1.E-02 1.E-01 1.E+00 1.E+01-20 Ionic Strength (M) 29

Megasonic Removal of Aminated Silica Particles in KCl Solutions of Different Concentration at Different Power Densities 0.43 W/cm2 (KCl) 0.43 W/cm2 (DI water) 0.077 W/cm2 (KCl) 100 90 80 ph = 6.0, T = 30 0 C 70 60 P R E % 50 40 30 20 10 0 1.E-08 1.E-07 1.E-06 1.E-05 1.E-04 1.E-03 1.E-02 1.E-01 1.E+00 1.E+01 Ionic Strength (M) 30

Critical Concentration of KCl for Removal of Aminated Silica at Different Power Densities Critical KCl Concentration (M) 1.0E+00 1.0E-01 1.0E-02 1.0E-03 1.0E-04 1.0E-05 0 0.1 0.2 0.3 0.4 0.5 Power density (W/cm 2 ) Critical concentration (Cc) is defined as the concentration at which 50 % particle removal efficiency (PRE) is achieved 31

Effect of Cleaning Time on Removal of Aminated Silica Particles PRE % 100 90 80 70 60 50 40 30 20 10 0 0.001 KCl (0.103 W/cm2) DI water (0.43 W/cm2) 0 1 2 3 4 5 6 Cleaning time (min) 32

Effect of KCl Concentration on Debye Potential 1.E-04 0.077 W/cm2 0.215 W/cm2 0.43 W/cm2 2.17 W/cm2 φ 0 = cu 0 (4Π / D w) [1 + ((4Π / D w ) ( n j ( n j m e j e 2 j j / / f f j j ) )) 2 ] 0.5 Potential (V) 1.E-05 1.E-06 1.E-07 1.E-05 1.E-04 1.E-03 1.E-02 1.E-01 KCl Concentration (M) Removal Force (10-3 M KCl and 2.17 W/cm 2 ) = 10-15 N Van der Waals Force = 3 * 10-10 N e i X f i (v i v 0 ) = m i (dv i /dt) Force Balance (1) (δn i / δt) + δ(n i v i )/ δt = 0 Continuity Equation (2) D (δx/ δx) = 4Π Σ (n j e j ) Poisson s Equation (3) e i is the charge on the ion, m i is the mass of the ion, f i is the friction coefficient, X is the electric field strength v i and v 0 are velocities of ion and solvent molecules, n i is the number of ions in a given volume D is the dielectric constant of the solvent 33

Computation of Force Due to Dipole Moment CVP Effect 6πv aς ε D = w m 0 v = solvent velocity Zeta Potential v = 2 I ρ c 1 0.5 Transducer Intensity Force on particle due to dipole moment mq' F = = 3 l Net charge displaced due to asymmetry of double layer Q' 2 l 2 Offset between the center of particle and the double layer r l Q' = Q 3 ( 4 / 3) π l' 3 ( 4 / 3) π r' 34

Magnitude of removal force, F, as a function of transducer power density for solution ionic strength of 10-4 M 1.0E-09 0.103 W/cm2 0.22 W/cm2 0.43 W/cm2 Force, F, (N) 1.0E-10 1.0E-11 1.0E-12 1.0E-13 0.2 0.4 0.6 0.8 1 1.2 Charge Offset Between the Particle and the Surrounding Ions, l, (nm) Van der waals Force Hamaker constant for SiO 2 and water taken as 6.2 *10-20 J and 4.4*10-20 J respectively Separation Distance between particle and wafer = 4 Å 35

HOW TO EXPLAIN THE EFFECT OF IONIC STRENGTH? Let total charge on the center mass and surrounding ionic cloud be + Q and Q respectively r l l =r Q = Q l = relative displacement between the center of particle and surrounding ions 3 ( 4 / 3) π l' Force, F = Q 2 / l 2 where Q' = Q 3 ( 4 / 3) π r' 2 Q' F ' = = 2 l' 2 Q l' 6 r' 4 36

Now, if the outer ionic cloud is compressed due to increase in solution ionic strength r l 3 ( 4 / 3) π l'' Force, F = Q 2 / l 2 where Q'' = Q 3 ( 4 / 3) π r'' 2 Q'' F '' = = 2 l'' 2 Q l'' 6 r'' 4 Removal force increases with increase of ionic strength 37

Separation of Electro-acoustic and Cavitation Effects 0.43 W/cm2 (KCl) 0.43 W/cm2 (DI water) 0.077 W/cm2 (KCl) 100 90 80 ph = 6.0, T = 30 0 C P R E % 70 60 50 40 Electro-acoustic only Electro-acoustic and Cavitation 30 20 10 0 1.E-08 1.E-07 1.E-06 1.E-05 1.E-04 1.E-03 1.E-02 1.E-01 1.E+00 1.E+01 Ionic Strength (M) 38

Summary Using simple electrolyte solutions, removal of positively charged silica particles from native oxide wafers in a megasonic field can be significantly improved by increasing solution ionic strength. Simple calculations have shown that depending on ionic strength and power density, CVP can exert a removal force that is equal to adhesive force on the particles. Hydrophone and sonoluminescence studies revealed that pressure amplitude of the sound wave can be increased in KCl solutions of concentration greater than 0.01 M. This higher pressure amplitude leads to more intense cavitation which could provide additional force for removal of particles. 39

Future Work Attempt to deconvolute the effect of cavitation from electroacoustic effect. This can be done using CO 2 that is known to suppress cavitation. The ionic strength of the solution can be modulated by controlling the amount of CO 2 dissolved. Carry out particle removal studies on patterned test structures. Relate particle removal to damage of structures. Study the effect of electrolytes for particles with varying degree of adhesion to surface. Investigate the degree of adhesion by atomic force microscopy measurements. 40

Acknowledgement Dr. Steven Verhaverbeke, Applied Materials (donation of hydrophone and wafers) Mark Beck, Prosys Megasonics (donation of Megasonic tank) Group: Nandini, Jovanny, Ashok and Raj 41