electrochemical aspects of copper chemical mechanical planarization (cmp )

1
Electrochemical Aspects of Copper Chemical Mechanical Planarization (CMP) Esta Abelev , D. Starosvetsky and Y. Ein-Eli. Introduction: Copper is used as a replacement of aluminum in integrated circuit interconnections. The advantages of copper interconnectors are based on two important properties of copper; higher electric conductivity and stronger electromigration resistance. opper Metallization Technology: I) Etching trenches and vias in ILD or low-k dielectric. (II) Deposition of diffusion barrier layer. ILD (b) Si (a) Si ILD (III) Copper deposition: Electroplating or Electroless. (c) ILD Si (IV) Global Planarization of the surface. ILD (d) Si Research objectives: To study and understand the electrochemical behavior and compatibility of copper CMP slurry solutions. Results: Ammonium hydroxide (NH 4 OH) Concentrat ion NH 4 OH E corr V SCE I corr mA/cm 2 Corrosi on Rate nm/min 2.35 g/l 0.315 29.76 1.313 30 g/l 0.509 51.93 2.29 2.35 g/l NH 3 30 g/l NH 3 1 min In solution 60 min In solution Active Copper Dissolution Nitric Acid (HNO 3 ) Concentrat ion pH E corr I corr Corrosi on Rate %wt HNO 3 V SCE mA/cm 2 mm/min 0.2 1.7 8 0.0 2 0.604 13.3 1 1.1 9 0.0 4 1.658 36.6 3 0.9 0.0 52 4.468 100.45 Active Copper Dissolution Nitric Acid (HNO 3 ) and Inhibitor (benzotriazole) N N N Cu N N N Cu Cu 10 -7 10 -6 10 -5 10 -4 10 -3 10 -2 0,0 0,1 0,2 3 w t% HNO 3 3 w t% HNO 3 + 0.02M BTA P otential( V SCE ) C urrent( A /cm 2 ) With Inhibitor (BTA) Without Inhibitor (BTA) Hydrogen Peroxide (H 2 O 2 ) Hydrogen Peroxide (H 2 O 2 ) and Inhibitor (benzotriazole) a) b) 10 -6 10 -4 10 -2 0.4 0.6 0.8 c b a Potential(V SC E ) C urrent(A /cm 2 ) Figure 6: Anodic potentiodynamic curves (Scan rate of 1 mV/s) of copper immersed in 3 vol% peroxide Solutions with and without the addition of buffer and Na2(SO4) additives: (a) without additives; (b) with 5 ml addition of buffer (pH 4); (c) with buffer and 10 g/l Na2SO4 (pH 4). 10 -8 10 -7 10 -6 10 -5 10 -4 10 -3 10 -2 0.0 0.2 0.4 0.6 0.8 1 m V/s A ddition 0.01M B TA plus 3 vol% H 2 O 2 A ddition 0.01M BTA 10g/lN a 2 SO 4 (H 2 SO 4 drop) pH 4.2 Potential(V SCE ) C urrent(A /cm 2 ) 10 -9 10 -8 10 -7 10 -6 10 -5 10 -4 10 -3 10 -2 0.0 0.2 0.4 0.6 1 m V/s R everse potential: 0.7V 0.1V 0.2V 0.35V 0.4V 0.5V Potential(V SCE ) C urrent(A /cm 2 ) 0 1000 2000 3000 4000 0.0 0.1 0.2 0.3 0.4 0.5 addition of H 2 O 2 E corr(V SCE ) Tim e (sec) Planarization is an important technological step in copper metallization. This research work is focused on problems associated with copper planarization technique-Chemical Mechanical Planarization (CMP). Conclusions All the proposed slurries (NH 4 OH, HNO 3 and H 2 O 2 ) do not provide the conditions required for conventional CMP: Copper is actively dissolved with a relatively high dissolution rate. • The active dissolution of Cu proceeds non- uniformly, with deep intergranular penetration. This may lead to a damage of the thin Cu layer, resulting in severe dents and fractures in the copper interconnects. • Copper protection with the use of inhibitors is not effective for CMP processes, [which continue only for a period of 2 minutes], under rapid surface abrading. • The use of oxidizers such as peroxide is not effective in conjugation with inhibitors. -0.6 -0.4 -0.2 0.0 0.2 0.4 10 -5 10 -4 10 -3 30 g/lN H 3 2.35 g/lN H 3 C urrent(A /cm 2 ) Potential(V SC E ) 0 1000 2000 3000 -0.6 -0.5 -0.4 -0.3 30 g/lN H 3 2.35 g/lN H 3 Ecorr(V SCE ) E xposure T im e (sec) Potential 0.2V 500 550 600 650 700 750 0 10 20 30 40 50 Current(m A /cm 2 ) Tim e (sec) A ddison ofBTA Potential 0.2V 500 550 600 650 700 750 0 10 20 30 40 50 Current(m A /cm 2 ) Tim e (sec) A ddison ofBTA 500 550 600 650 700 750 0 10 20 30 40 50 Current(m A /cm 2 ) Tim e (sec) A ddison ofBTA Addition of BTA Potential 0.1V Potential 0.1V Addition of BTA Corrosion & Applied Electrochemistry Laboratory (CAEL) Department of Materials Engineering, Technion, Haifa 32000, Israel. Figure 1: a) Corrosion potential transient of copper in 2.35 g/l (●) and 30 g/l NH 3 g/l (○) solutions at 25 °C, b) Polarization curves of copper electrodes obtained in 2.35 g/l (●) and 30 g/l (○) NH 3 at scan rate of 1 mV/s. : a), b) SEM micrographs obtained after one hour exposure at OCP in 3 vol.% nitric acid solution. a) b) a) b) Figure 3: a) Anodic potentiodynamic curves (scan rate 1 mV/sec) of copper in 3 vol.% nitric acid without (●) and with (○) 0.02 M BTA, b) Anodic current transient of copper measured in 3 vol.% nitric acid containing 0.02 M BTA (at applied voltage of 0.1 V). 10 -7 10 -6 10 -5 0.3 0.4 0.5 0.6 15 vol.% 3 1 Potential(V SCE ) C urrent(A /cm 2 ) 4: Anodic potentiodynamic curves of copper obtained immediately mmersion in 1, 3, and 15 vol % peroxide solutions at a scan rate of 1 mV/s. 5: Two fragments of copper surface after one hour exposure at the OCP in 3 vol.% de solution. Figure 8: Potentiodynamic profiles (scan rate of 1 mV/s) of copper electrode immersed in three solutions; [a] solutions of Na 2 SO 4 peroxide-free; [b] Na 2 SO 4 with the addition of 0.01M BTA; [c] Na 2 SO 4 solution containing both BTA (0.01M) and peroxide 3% (vol). Figure 7: Corrosion potential transient of copper in 10 g/l Na 2 SO 4 and 0.01M BTA solution with addition of 3 vol.% H 2 O 2 . a b c Figure 10: Potentiodynamic profiles (scan rate of 1 mV/s) of copper electrode immersed in solution containing Na 2 SO 4 and 0.01M BTA. Copper electrode potential was swept back at potentials ranging between 0.1-0.7 V. Active Copper Dissolution (a) 0.1V 5m in Polished (b) (c) (d) (e) 0.3V 5m in 0.3V 5m in 0.4V 5m in 0.4V 5m in

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Cu. Addition of BTA. Cu. N. N. N. N. Potential 0.1V. N. N. Cu. a). b). Addition of BTA. Potential 0.1V. Electrochemical Aspects of Copper Chemical Mechanical Planarization (CMP ). Esta Abelev , D. Starosvetsky and Y. Ein-Eli. Corrosion & Applied Electrochemistry Laboratory (CAEL) - PowerPoint PPT Presentation

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Page 1: Electrochemical Aspects of Copper Chemical Mechanical Planarization (CMP )

Electrochemical Aspects of Copper Chemical Mechanical Planarization (CMP)Esta Abelev, D. Starosvetsky and Y. Ein-Eli.

Introduction:Copper is used as a replacement of aluminum in integrated circuit interconnections. The advantages of copper interconnectors are based on two important properties of copper; higher electric conductivity and

stronger electromigration resistance.

Copper Metallization Technology:(I) Etching trenches and vias in ILD or low-k dielectric.

(II) Deposition of diffusion barrier layer.

ILD (b) Si

(a) Si

ILD

(III) Copper deposition: Electroplating or Electroless.

(c) ILD

Si

(IV) Global Planarization of the surface.

ILD (d) Si

Research objectives: To study and understand the electrochemical behavior and compatibility of copper CMP slurry solutions. Results:Ammonium hydroxide (NH4OH)

ConcentrationNH4OH

Ecorr

VSCE

Icorr

mA/cm2

Corrosion Rate

nm/min

2.35 g/l 0.315 29.76 1.313

30 g/l 0.509 51.93 2.29

2.35 g/l NH3 30 g/l NH3

1 minIn solution

60 minIn solutionActive Copper Dissolution

Nitric Acid (HNO3)

Concentration pH Ecorr IcorrCorrosion Rate

%wt HNO3 VSCE mA/cm2 mm/min

0.2 1.78 0.02 0.604 13.3

1 1.19 0.04 1.658 36.6

3 0.9 0.052 4.468 100.45

Active Copper Dissolution

Nitric Acid (HNO3) and Inhibitor (benzotriazole)

N

N

N

Cu

N

N

N

Cu

Cu

10-7 10-6 10-5 10-4 10-3 10-2

0,0

0,1

0,2

3 wt% HNO3

3 wt% HNO3 + 0.02M BTA

neat 3% wt HNO3

3% wt HNO3 + 0.02M BTA upon immersion

3% wt HNO3 + 0.02M BTA after 1hr in solution

B D F

Pote

ntia

l ( V

SCE )

Current ( A/cm2 )

With Inhibitor (BTA) Without Inhibitor (BTA)

Hydrogen Peroxide (H2O2)

Hydrogen Peroxide (H2O2) and Inhibitor (benzotriazole)

a) b)

10-6 10-4 10-2

0.4

0.6

0.8 cba

3% wt H2O

2No Pretreatment

Scan Rate 5mV/s: 3% wt H

2O

2 3% wt H

2O

2 + Buffer pH 4

3% wt H2O

2 + Buffer pH 4 + 10g/l Na

2SO

4

Pote

ntia

l (V

SCE)

Current (A/cm2)

B B B

Figure 6: Anodic potentiodynamic curves (Scan rate of 1 mV/s) of copper immersed in 3 vol% peroxide Solutions with and without the addition of buffer and Na2(SO4) additives: (a) without additives; (b) with 5 ml addition of buffer (pH 4); (c) with buffer and 10 g/l Na2SO4 (pH 4).

10-8 10-7 10-6 10-5 10-4 10-3 10-2

0.0

0.2

0.4

0.6

0.81 mV/s

Addition 0.01M BTA plus 3 vol% H2O2

Addition 0.01M BTA

10g/l Na2SO4 (H2SO4 drop) pH 4.2

Cu, Scan rate 1 mV/s, upon immersion

Pote

ntia

l (V

SCE)

Current (A/cm2)

B D F

10-9 10-8 10-7 10-6 10-5 10-4 10-3 10-2

0.0

0.2

0.4

0.6

1 mV/s

files:CV_x(V)

Cu, 10g/l Na2SO

4 (H

2SO

4 drop) + 0.01M BTApH 4.3

Upon immersion, scan rate 1 mV/sDifferent reverse potentials

Reverse potential: 0.7V 0.1V 0.2V 0.35V 0.4V 0.5V

Pote

ntia

l (V

SCE)

Current (A/cm2)

B D01 L02 P035 R04 B

0 1000 2000 3000 4000

0.0

0.1

0.2

0.3

0.4

0.5

Cu, 10g/l Na2SO

4 (H

2SO

4 drop) pH 4.3

addition of H2O

2

Ecor

r (V

SCE)

Time (sec)

B

Planarization is an important technological step in copper metallization. This research work is focused on problems associated with copper planarization technique-Chemical Mechanical Planarization (CMP).

Conclusions

• All the proposed slurries (NH4OH, HNO3 and H2O2) do not provide the conditions required for conventional CMP:

Copper is actively dissolved with a relatively high dissolution rate.

• The active dissolution of Cu proceeds non-uniformly, with deep intergranular penetration. This may lead to a damage of the thin Cu layer, resulting in severe dents and fractures in the copper interconnects.

• Copper protection with the use of inhibitors is not effective for CMP processes, [which continue only for a period of 2 minutes], under rapid surface abrading.

• The use of oxidizers such as peroxide is not effective in conjugation with inhibitors.

-0.6

-0.4

-0.2

0.0

0.2

0.4

10-5 10-4 10-3

30 g/l NH3

2.35 g/l NH3

1 mV/s

2.35 g/l NH3

30 g/l NH3

No pretreatment Upon immertionScan rate 1 mV/s

Current (A/cm2)

Pote

ntia

l (V

SCE)

E C A C

0 1000 2000 3000-0.6

-0.5

-0.4

-0.3

30 g/l NH3

2.35 g/l NH3 2.35 g/l NH

3 30 g/l NH

3

Ecor

r (V

SCE)

Exposure Time (sec)

B B

Potential 0.2V

500 550 600 650 700 7500

10

20

30

40

50

Curre

nt (m

A/c

m2 )

Time (sec)

B

Addison of BTA

Potential 0.2V

500 550 600 650 700 7500

10

20

30

40

50

Curre

nt (m

A/c

m2 )

Time (sec)

B

Addison of BTA

500 550 600 650 700 7500

10

20

30

40

50

Curre

nt (m

A/c

m2 )

Time (sec)

B

Addison of BTAAddition of BTA

Potential 0.1VPotential 0.1V

Addition of BTA

Corrosion & Applied Electrochemistry Laboratory (CAEL)Department of Materials Engineering, Technion, Haifa 32000, Israel.

Figure 1: a) Corrosion potential transient of copper in 2.35 g/l (●) and 30 g/l NH3 g/l (○) solutions at 25 °C, b) Polarization curves of copper electrodes obtained in 2.35 g/l (●) and 30 g/l (○) NH3 at scan rate of 1 mV/s.

Figure 2: a), b) SEM micrographs obtained after one hour exposure at OCP in 3 vol.% nitric acid solution.

a) b)

a) b)

Figure 3: a) Anodic potentiodynamic curves (scan rate 1 mV/sec) of copper in 3 vol.% nitric acid without (●) and with (○) 0.02 M BTA,b) Anodic current transient of copper measured in 3 vol.% nitric acid containing 0.02 M BTA (at applied voltage of 0.1 V).

10-7 10-6 10-5

0.3

0.4

0.5

0.6

15 vol.%

3

1

H2O

2 concentration : 1% wt 3% wt 15% wt

B D F

Pote

ntia

l (V

SCE)

Current (A/cm2)Figure 4: Anodic potentiodynamic curves of copper obtained immediately upon immersion in 1, 3, and 15 vol % peroxide solutions at a scan rate of 1 mV/s.

Figure 5: Two fragments of copper surface after one hour exposure at the OCP in 3 vol.% peroxide solution.

Figure 8: Potentiodynamic profiles (scan rate of 1 mV/s) of copper electrode immersed in three solutions; [a] solutions of Na2SO4 peroxide-free; [b] Na2SO4 with the addition of 0.01M BTA; [c] Na2SO4 solution containing both BTA (0.01M) and peroxide 3% (vol).

Figure 7: Corrosion potential transient of copper in 10 g/l Na2SO4 and 0.01M BTA solution with addition of 3 vol.% H2O2.

ab

c

Figure 10: Potentiodynamic profiles (scan rate of 1 mV/s) of copper electrode immersed in solution containing Na2SO4 and 0.01M BTA. Copper electrode potential was swept back at potentials ranging between 0.1-0.7 V.

Active Copper Dissolution

(a) 0.1V 5min Polished

(b) (c)

(d) (e)

0.3V 5min 0.3V 5min

0.4V 5min 0.4V 5min