Scale-Up Activities in Atomic Layer Deposition at Argonne Jeffrey Elam, Anil Mane, Joe Libera December 9, 2011 Large Area Picosecond Photodetector Collaboration Meeting December 9-10, 2011, Argonne National Laboratory
Dec 31, 2015
Scale-Up Activitiesin Atomic Layer Deposition at
Argonne
Jeffrey Elam, Anil Mane, Joe LiberaDecember 9, 2011
Large Area Picosecond Photodetector Collaboration MeetingDecember 9-10, 2011, Argonne National Laboratory
Outline
Introduction to ALD (1 slide) ALD on 33mm plates Challenges with scale-up to larger substrates Conclusions
2
AlCH3
CH3
CH3OH OH OH
AlCH3
CH3
CH3
A)
B)
OHAl(CH3)3OH OH
Trimethyl Aluminum(TMA)
CH4
AlCH3
AlCH3CH3
H2OAl
CH3
CH3
CH3OH OH OH
AlCH3
AlCH3CH3 Al
CH3
CH3
CH3
CH3
OH OH OHAl Al
CH3CH3
H2O
H2OOH
CH4
OHOH
Binary Reaction Sequence for Al2O3 ALD
1 ALD Cycle of TMA/H2O Deposits 1 Al2O3 “Monolayer”
3
4
Multiple 33mm MCPs in Tubular ALD Reactor
•Thickness uniformity on monitor Si(100) <2%• The resistive layer thickness ~800A• Similar thickness trend observed on second batch of 5 MCPs Excellent batch-to-batch reproducibility
Chem-2 Resistive Coating
5
Resistance Comparison for 9 MCPs (air vs. vacuum)
• Average resistance (2 batches of 5 plates)115 ±12 M ~10% resistance variation
Chem-2 Resistive Coating
Challenges to Coating Larger Areas
Need a bigger reactor Non-ideal ALD surface reactions High aspect ratios High surface areas
6
Large Substrate Reactor
From 1x1-in plates to 12-in x 18-in plates
7
2” tube
12x18” box
Coating 8” MCPs in Beneq
8
300 mm chamber
Non-Ideal ALD Surface Reactions
9
InCp + O3 →In2O3
In2O3 O3 O* + O2
Indium oxide catalyzes ozone destruction
In2O3 films were thinner downstream in reactor
In2O3 ALD in Large Substrate Reactor
Scale-up of ALD In2O3 to 12”x18” Substrates
InCp + H2O + O2InCp + O3
Thickness deviation: 2.5% Resistivity deviation: 6%
Thickness deviation: 45%
10
Non-self limiting ALD reactions can lead to non-uniform films in larger ALD systems
15 μm
0
10
20
30
40
50
60
70
0 10 20 30 40 50 60 70
Tun
gste
n E
DA
X S
ign
al
Distance (Microns)
Conformal coating on all exposed surfaces Aspect ratio ~ 1000
40 nm pores, 70 microns long
11
Coating High Aspect Ratios: ALD W in Anodic Alumina
Large Substrate Surface Area: Silica Gel Powder 100 micron particles, 30 nm pores (aspect ratio ~ 2000)
Surface area = 100 m2/g Powder bed fixture for ~1 g support
12
Self-Limiting Al2O3 ALD
Self-limiting growth on planar and porous surfaces
Exposures increased by x100
0
0.5
1
1.5
0 0.05 0.1 0.15 0.2
Al 2
O3 G
row
th R
ate
(Å/C
ycle
)
TMA Exposure (Torr s)
Silica GelPlanar Surface
0
1
2
3
0 5 10 15 20 25
Wei
ght
Gai
n (
%)
TMA Exposure (Torr s)
13
Surface Areas of Glass Capillary Arrays:
14
MCP Type d (µm) γ = l/d α ATotal (cm2)33mm diam 40 40 0.65 881
40 40 0.83 1,120 20 60 0.65 1,317
8in square 40 40 0.65 43,244 20 60 0.65 64,712
(thanks Jason M.)
Empty tube reactor: ~2000cm2
Empty LSR: ~4000 cm2
Empty Beneq 300mm: ~1600 cm2
MCP aspect ratio = 60 (we’ve done 10^5)
8” MCP surface area = 6.5 m2 (we’ve done 10^3)
Piece of cake…
Work Plan
15
1) Qualify Beneq for Chem2 coatings using coupons and 33mm MCPs in new 300mm chamber
2) Coat single 8”x8” MCPs in 300 mm chamber
200 mm chamber
3) Coat multiple (1-4) 8”x8” MCPs in 300 mm chamber
X) Coat multiple (20) 8”x8” MCPs in 3D chamber
300 mm chamber
<1% non-uniformity in 100 nm coating
16
Al2O3 ALD in 300 mm Reactor
Works great!
Chem-2 ALD in 300 mm Reactor
17
Test Metrics:•Optimized chemistry -2 baseline process on 300mm chamber:•Deposit 300mm wafer at same condition as MCP deposition.•Evaluated the resistivity uniformity across the large area
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
Precursor inlet
direction
300mm
Resistivity of Chem2 coating at different locations on 300mm wafer
18
0 5 10 15 20 25 30
2.00x109
4.00x109
6.00x109
8.00x109
1.00x1010
Res
istiv
ity(o
hm-c
m)
Location on wafer
Works great for Chem-2!
Chem-2 thickness NU on 300mm wafer with 8”x8” MCP on top:2D thickness map
19
Items Run-3
Average (nm) 42.905
STDV 4.484
1sigma 0.105
%sigma 10.450
Max (nm) 57.821
Min(nm) 36.843
% diff 48.893
-100 -50 0 50 100
-100
-50
0
50
100
Y
X
36.80
39.44
42.08
44.71
47.35
49.99
52.63
55.26
57.90
•We may need square chamber?
300m
m
300mm
1-sigma thickness: 10%
August 22, 2011
8” 40µm MCP Pair Gain Map
Y gain slice
X gain slice
Y gain slice
FIRST Gain map – Looks awful - multifiber visible, lots of gain non-uniformityThis is from the thickness non-uniformity
(thanks Ossy, Jason, SSL)
20
21
300 mm wafer
8” MCP
reactor wall
Troubleshooting in Beneq
Top View
Side View
ALD conductive coating with MCP substrate installed over Si(100) 300 mm wafer
Measure film thickness on Si wafer using 4-point probe conductivity (easy, quantitative)
assumed flow distribution
Process testing on 8” MCP on Beneq
22
Items Thickness data from Resistance
Average (nm) 75.169
STDV 3.412
1sigma 0.045
%sigma 4.539
Max(nm) 78.186
Min(nm) 63.107
% diff 20.060
-100 -50 0 50 100
-100
-50
0
50
100
YX
63.10
64.99
66.88
68.76
70.65
72.54
74.43
76.31
78.20
Precursor inlet
• Baseline process: 50 cycles conductive coating (No MCP)
1-sigma = 4%
Thickness values form resistance and 2D map:
23
Items Baseline Run-1 Run-2 Run-3 Run-3# of cycles 50cycles 50cycles 30cycles 30cycles 25cycles
Expected thickness (nm) 75 75 45 45 37
Dose time (s) 1 10 20 40 60
Average (nm) 75.169 56.289 25.263 42.905 35.491
G (nm/cycle) 1.50 1.13 0.842 1.43 1.42
STDV 3.412 32.299 13.352 4.484 8.448
1sigma 0.045 0.574 0.529 0.105 0.238
%sigma 4.539 57.381 52.851 10.450 23.804
Max (nm) 78.186 110.438 46.746 57.821 47.500
Min(nm) 63.107 0.236 2.196 36.843 14.884
% diff 20.060 195.776 176.348 48.893 91.900
-100 -50 0 50 100
-100
-50
0
50
100
Y
X
63.10
64.99
66.88
68.76
70.65
72.54
74.43
76.31
78.20
-100 -50 0 50 100
-100
-50
0
50
100
Y
X
0.000
13.81
27.63
41.44
55.25
69.06
82.88
96.69
110.5
-100 -50 0 50 100
-100
-50
0
50
100
Y
X
2.000
7.600
13.20
18.80
24.40
30.00
35.60
41.20
46.80
-100 -50 0 50 100
-100
-50
0
50
100
Y
X
36.80
39.44
42.08
44.71
47.35
49.99
52.63
55.26
57.90
-100 -50 0 50 100
-100
-50
0
50
100
Y
X
14.80
18.89
22.98
27.06
31.15
35.24
39.32
43.41
47.50
Tested many ideas, hardware, software, reactor breaks, etc. (3 months)
1-sigma = 4% 57% 52% 10% 24%
24
Troubleshooting in Beneq: Al2O3
Side View
ALD Al2O3 coating with MCP substrate installed over Si(100) 300 mm wafer
Visually assess coating uniformity
Measure film thickness on Si using ellipsometry
Troubleshooting in Beneq: Al2O3
Anil: “We have a flow problem… we need a square chamber”
50 nm
100 nm
150 nm
Precursor inlet
25
Si
MCP
Troubleshooting in Tubular Reactor
26
2cm x 30 cm Si(100) substrate, rest 2x20cm MCP 2 mm above Si500 cycles TMA/H2O for Al2O3
• Narrow gap under MCP• High surface area
2 inches
26
Troubleshooting in Tubular Reactor
27
2-5-2-5, 0.05 Torr doses
2-5-2-5, 0.2 Torr doses
2-5-2-5, 1 Torr doses
Some non-uniformity, not as bad as Beneq
Si
MCP
Si
Troubleshooting in Tubular Reactor
• Narrow gap under MCP• Narrow gap over MCP• High surface area
28
Troubleshooting in Tubular Reactor
2-5-2-5, 0.05 Torr doses
Same bad non-uniformity as in the Beneq
29
30
Si
Si
Troubleshooting in Tubular Reactor
2-5-2-5, 0.05 Torr doses
Nearly perfect uniformity
• Narrow gap under MCP”• Narrow gap over MCP• No high surface area
300 mm wafer
8” MCP
reactor wall
What is going wrong in Beneq?
Top View
Side View
actual flow distribution
• Narrow gap under MCP• Narrow gap over MCP• High surface area
• No flow in the gap• Slow outgassing/diffusion from MCP• Precursors mix, CVD
31
The problem: flow is bypassing the MCP Solution: we need to confine the flow so that
it is forced to pass in the gap between the plate(s) and the reactor wall.
We have a flow problem… we need a square reactor.
What is going wrong in Beneq?
50 nm
100 nm
150 nm
Precursor inlet
32
300 mm wafer
8” MCP
reactor wall
Potential Solution, Conclusions
Top View
Side View
Equal gap
Convert circle into square
CFD modeling would be helpful
Listen to Anil33