Monitoring Air Supply in Spin Coating Photolithography Process · 2018-08-14 · Monitoring Air...
Transcript of Monitoring Air Supply in Spin Coating Photolithography Process · 2018-08-14 · Monitoring Air...
ADVANCED MATERIALS HANDLING | APPLICATION NOTE
Monitoring Air Supply in Spin Coating Photolithography ProcessAuthor: Kanjanawadee Shiraishi, Entegris
Photoresist film uniformity is one important factor among many
when spin coating photoresist. To control the uniformity of the
photoresist film, fluid flow at the dispense point plays an import-
ant role. To ensure uniform topography, fluid must form a
straight, solid stream at the nozzle tip, and it must flow at a
constant flow rate. Controlling fluid flow at the nozzle tip can
be achieved by adjusting the open and close timing of a stop
suckback valve that is usually installed between the dispense
pump and nozzle. After the dispense pump dispenses the fluid,
the stop suckback valve needs to open at the right time to enable
the fluid to form a straight, solid stream. If the valve opens too
early, there is not enough pressure to form a solid fluid stream
and the fluid will drip out of the nozzle tip. If the valve opens too
late, the flow rate will be compromised and too much fluid will
flow at the beginning, and too little will flow at the end.
Equally important to opening at the right time, the valve needs
to close at the right time as well. If the valve closes too early,
there will be an insufficient amount of fluid to cover the whole
wafer. If the valve closes too late, there may be a drop of fluid
that dispenses after the main fluid stream stops flowing because
the valve is not yet closed. To prevent these undesirable events,
the open and close timing of the stop suckback valve must be
precisely controlled.
Though most stop suckback valves are digitally controlled,
some are pneumatically controlled and require air to open and
close them. Air-operated valves need very consistent air pressure
to control the valve actuation and avoid fluctuations between
dispense cycles. Supplying consistent air pressure to lithography
production processes is vital but not easy to achieve. Air pressure
fluctuation is often inevitable, particularly when too many devices
require air at the same time. In those instances, it is likely the
stop suckback valve could receive insufficient air supply than
is necessary to actuate it. This consequently leads to a delay in
opening and closing the valve, which will eventually cause
poor uniformity of photoresist film on wafers during the
coating process.
To monitor photoresist dispense uniformity, Entegris offers a
dispense pump with an integrated monitoring “confirmation tool”.
The confirmation tool confirms whether the last dispense has the
same characteristic as the reference dispense that is recorded
prior as a good dispense. If the stop suckback valve open and
close timing varies due to fluctuating air pressure, the confirma-
tion tool can detect the change in the fluid flow rate and alert the
operator before wafers are compromised.
This application note introduces four of the nineteen tools in
Entegris’ confirmation tool that are responsive when air supplied
to the external stop suckback valve is weakened.
FOUR RESPONSIVE TOOLS AND THEIR PRINCIPLES—
Pressure Profile Compare (%)
Compares the pressure profile of the last cycle to the reference.
The matching percentage enables user to identify if they can
achieve the same quality of dispense in the last cycle as in the
reference.
Maximum Dispense Pressure (psi)
Measures the maximum level of pressure in the dispense cham-
ber. Observing a maximum pressure difference between the
reference cycle and the last cycle enables user to control
dispense quality.
Average Pressure (psi)
Monitors the average level of pressure in the dispense chamber
during dispense. Observing the average pressure difference
between the reference and the last cycle enables user to control
the dispense quality and be aware when an abnormal event
occurs.
Maximum Pressure Time (ms)
Monitors the timing of the peak pressure in the dispense chamber
during dispense. Observing the timing difference between the
reference and the last cycle enables user to be aware when an
abnormal event occurs.
2
EXPERIMENT
—Testing was performed in the Entegris laboratory using
an IntelliGen® LV pump with firmware “V1005_987”
installed with Impact® 2 OF UPE 3 nm filter. Isopropyl
Alcohol (IPA) and 193 nm BARC were used as the
process fluids.
The event of weak air supplied to the external stop
suckback valve was created by installing a needle
valve to the pneumatic line, and then incrementally
closing the needle valve to decrease the amount
of air going to the valve. The detailed test setup is
shown in Figure 1.
Original air pressure supply to the external stop
suckback valve was set at 350 kPa (50.76 psi),
300 kPa (43.51 psi) and 250 kPa (36.26 psi) using a
pressure regulator. The needle valve was adjusted
to the following four conditions at each pressure
level: 1) Fully open, 2) ¼ closed, 3) ½ closed, and
4) ¾ closed. The actual air pressure was monitored by
a Keyence pressure sensor and the test values of the
four confirmation tools of the IntelliGen IG-ULV were
observed and recorded.
Tubing configuration
Location ID × length
Bottle to pump inlet 1/4" 70 cm
Pump outlet to flow sensor 1/4" 50 cm
Flow sensor to air operating valve 1/4" 70 cm
Air operating valve to nozzle 2 mm × 100 cm
Vent line 2 mm × 50 cm
RESULT AND DISCUSSION
—Test results are divided into two parts, 1) Confirmation
whether air supplied to the external stop suckback
valve is weakened when the needle valve is closed,
and 2) Results of the four confirmation tools: Pressure
Profile Compare, Maximum Dispense Pressure,
Average Pressure, and Maximum Pressure Time.
1. Confirmation whether air supplied to the external
stop suckback valve is weakened when needle valve
is closed:
350 kPa (50.76 psi) is the pressure specification.
Normally, users are required to provide this level of
pressure to the stop suckback valve. 300 kPa (43.51)
and 250 kPa (36.26 psi) are the test cases when air
supply is lower than the requirement.
The confirmation shows that air supplied to the
outlet valve starts to become weak when the needle
valve (installed at the air line between the pressure
regulator and pneumatic valve) is half closed.
Figures 2 through 4 demonstrate the pressure
monitored by Keyence pressure sensor.
Figure 1. Test setup.
IPA 1 L Impact 2 V2 3 nm UPC UC
Flow sensor
Vent
Pump outlet
IG-ULV
Inlet
Air operating valve
Needle valve1⁄4, 1⁄2, 3⁄4 close
3
400
350
300
250
200
150
100
50
0
-50
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
350 kPa Air Supply with Fully Opened Needle Valve
PressureValve signal
25
20
15
10
5
-5
0
42
:16
.0
42
:16
.6
42
:17.
1
42
:17.
7
42
:18
.2
42
:18
.8
42
:19
.4
42
:19
.9
42
:20
.5
42
:21.
0
42
:21.
6
42
:22
.2
42
:22
.7
42
:23
.3
42
:23
.8
42
:24
.4
42
:25
.0
42
:25
.5
42
:26
.1
42
:27.
2
16:1
4.8
16:1
5.3
400
350
300
250
200
150
100
50
0
-50
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
350 kPa Air Supply with 1⁄4 Closed Needle Valve
PressureValve signal
25
20
15
10
5
-5
0
05
:14
.0
05
:14
.6
05
:15
.1
05
:15
.7
05
:16
. 2
05
:16
.8
05
:17.
4
05
:17.
9
05
:18
.5
05
:19
.0
05
:19
.6
05
:20
.2
05
:20
.7
05
:21.
3
05
:21.
8
05
:22
.4
05
:23
.0
05
:23
.5
05
:24
.1
05
:24
.6
05
:25
.2
05
:25
.8
05
:26
. 3
400
350
300
250
200
150
100
50
0
-50
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
350 kPa Air Supply with 1⁄2 Closed Needle Valve
PressureValve signal
25
20
15
10
5
-5
0
27:
27.
0
27:
27.
6
27:
28
.1
27:
28
.7
27:
29
.2
27:
29
.8
27:
30
.3
27:
30
.9
27:
31.
4
27:
32
.0
27:
32
.5
27:
33
.1
27:
33
.7
27:
34
.2
27:
34
.8
27:
35
.3
27:
35
.9
27:
36
.4
27:
37.
0
27:
37.
5
27:
38
.1
32
:33
.7
32
:34
.2
400
350
300
250
200
150
100
50
0
-50
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
350 kPa Air Supply with 3⁄4 Closed Needle Valve
PressureValve signal
25
20
15
10
5
-5
0
49
:16
.0
49
:16
.5
49
:17.
1
49
:17.
6
49
:18
.1
49
:18
.7
49
:19
.2
49
:19
.7
49
:20
.3
49
:20
.8
49
:21.
4
49
:21.
9
49
:22
.4
49
:23
.0
49
:23
.5
49
:24
.0
49
:24
.6
49
:25
.1
49
:25
.6
49
:26
. 2
49
:26
.7
02
:53
.2
02
:53
.8
Figure 2. Actual pressure (blue) and valve signal (red) monitored by Keyence at air supply of 350 kPa.
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
300 kPa Air Supply with Fully Opened Needle Valve
PressureValve signal
06
:23
.0
06
:23
.5
06
:24
.0
06
:24
.6
06
:25
.1
06
:25
.6
06
:26
.1
06
:26
.6
06
:27.
2
06
:27.
7
06
:28
.2
06
:28
.7
06
:29
.2
06
:29
.8
06
:30
.3
06
:30
.8
06
:31.
3
06
:31.
8
06
:32
.4
06
:32
.9
06
:33
.4
06
:33
.9
06
:34
.4
350
300
250
200
150
100
50
0
-50
350
300
250
200
150
100
50
0
-50
350
300
250
200
150
100
50
0
-50
350
300
250
200
150
100
50
0
-50
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
300 kPa Air Supply with 1⁄4 Closed Needle Valve
PressureValve signal
25
20
15
10
5
-5
0
25
20
15
10
5
-5
0
25
20
15
10
5
-5
0
25
20
15
10
5
-5
0
25
:54
.0
25
:54
.5
25
:55
.0
25
:55
.5
25
:56
.0
25
:56
.5
25
:57.
0
25
:57.
5
25
:58
.0
25
:58
.5
25
:59
.0
25
:59
.6
26
:00
.1
26
:00
.6
26
:01.
1
26
:01.
6
26
:02
.1
26
:02
.6
26
:03
.1
26
:03
.6
10:5
8.1
10:5
8.6
10:5
9.1
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
300 kPa Air Supply with 1⁄2 Closed Needle Valve
PressureValve signal
49
:56
.0
49
:56
.5
49
:57.
0
49
:57.
5
49
:58
.0
49
:58
.4
49
:58
.9
49
:59
.4
49
:59
.9
50
:00
.4
50
:00
.9
50
:01.
4
50
:01.
9
50
:02
.4
50
:02
.9
50
:03
.4
50
:03
.8
50
:04
.3
50
:04
.8
50
:05
.3
50
:05
.8
50
:06
.3
50
:06
.8
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al300 kPa Air Supply with 3⁄4 Closed Needle Valve
PressureValve signal
12:1
0.0
12:1
0.5
12:1
1.1
12:1
1.6
12:1
2.1
12:1
2.6
12:1
3.2
12:1
3.7
12:1
4.2
12:1
4.7
12:1
5.3
12:1
5.8
12:1
6. 3
12:1
6.8
12:1
7.3
12:1
7.9
12:1
8.4
12:1
8.9
12:1
9.4
12:2
0.0
12:2
0.5
12:2
1.0
58
:50
. 6
Figure 3. Actual pressure (blue) and valve signal (red) monitored by Keyence at air supply of 300 kPa.
4
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
250 kPa Air Supply with Fully Opened Needle Valve
PressureValve signal
28
:34
.0
28
:34
.6
28
:35
.1
28
:35
.7
28
:36
.3
28
:36
.8
28
:37.
4
28
:38
.0
28
:38
.6
28
:39
.1
28
:39
.7
28
:40
.3
28
:40
.8
28
:41.
4
28
:42
.0
28
:42
.6
28
:43
.1
43
:23
.7
43
:24
.3
43
:24
.8
43
:25
.4
43
:26
.0
43
:26
.5
300
250
200
150
100
50
0
-50
300
250
200
150
100
50
0
-50
300
250
200
150
100
50
0
-50
300
250
200
150
100
50
0
-50
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
250 kPa Air Supply with 1⁄4 Closed Needle Valve
PressureValve signal
25
20
15
10
5
-5
0
25
20
15
10
5
-5
0
25
20
15
10
5
-5
0
25
20
15
10
5
-5
0
50
:08
.0
50
:08
.5
50
:09
.1
50
:09
.6
50
:10
.2
50
:10
.7
50
:11.
3
50
:11.
8
50
:12
.4
50
:12
.9
50
:13
.5
50
:14
.0
50
:14
.5
50
:15
.1
50
:15
.6
50
:16
.2
50
:16
.7
50
:17.
3
50
:17.
8
58
:40
.4
58
:40
.9
58
:41.
4
58
:42
.0
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
250 kPa Air Supply with 1⁄2 Closed Needle Valve
PressureValve signal
12:4
6.0
12:4
6.6
12:4
7.3
12:4
7.9
12:4
8.5
12:4
9.2
12:4
9.8
12:5
0.4
12:5
1.0
12:5
1.7
12:5
2.3
12:5
2.9
12:5
3.6
12:5
4.2
12:5
4.8
12:5
5.5
12:5
6.1
12:5
6.7
17:4
0.3
17:4
1.0
17:4
1.6
17:4
2.2
17:4
2.9
Pre
ssu
re in
Pn
eum
atic
Lin
e (p
si)
Val
ve S
ign
al
250 kPa Air Supply with 3⁄4 Closed Needle Valve
PressureValve signal
35
:01.
0
35
:01.
6
35
:02
.1
35
:02
.7
35
:03
.2
35
:03
.8
35
:04
.4
35
:04
.9
35
:05
.5
35
:06
.0
35
:06
.6
35
:07.
2
35
:07.
7
35
:08
.3
35
:08
.8
35
:09
.4
35
:10
.0
35
:10
.5
35
:11.
1
35
:11.
6
38
:46
.2
38
:46
.8
38
:47.
3
Figure 4. Actual pressure (blue) and valve signal (red) monitored by Keyence at air supply of 250 kPa.
2. Test results of four confirmation tools: Pressure
Profile Compare, Maximum Dispense Pressure,
Average Pressure, and Maximum Pressure Time.
Results show that the four confirmation tools give a
reliable response to the situation when air supplied
to the external stop suckback valve is weaker than
the reference situation. Figures 5 through 8 show
the test results of Pressure Profile Compare, Maxi-
mum Dispense Pressure, Average Pressure, and
Maximum Pressure Time at the air supply of 350
kPa, 300 kPa, and 250 kPa, respectively. Figures 9
through 11 show the pressure profile when the
needle valve is fully opened, ¼ closed, ½ closed,
and ¾ closed, respectively.
5
Dis
pen
se P
ress
ure
(%)
350 kPa Dispense Pressure Profile Compare
120
100
80
60
40
20
0
Dis
pen
se P
ress
ure
(%)
120
100
80
60
40
20
0
Dis
pen
se P
ress
ure
(%)
120
100
80
60
40
20
0
300 kPa Dispense Pressure Profile Compare
250 kPa Dispense Pressure Profile Compare
0 100 200 300 400 500
Running Number
0 100 200 300 400 500
Running Number
0 100 200 300 400 500
Running Number
Top: Original air supply is at 350 kPa
Bottom: Original air supply is at 300 kPa
Top: Original air supply is at 250 kPa
Figure 5. Test results of Pressure Profile Compare Confirmation tool; Running No. 1 to 100: needle valve is fully opened, Running No. 101 to 200: needle valve is ¼ closed, Running No. 201 to 300: needle valve is ½ closed, Running No. 301 to 400: needle valve is ¾ closed and Running No. 401 to 500: needle valve is fully opened again.
Dis
pen
se P
ress
ure
(psi
)
350 kPa Dispense Maximum Pressure
17
16
15
14
13
12
11
Dis
pen
se P
ress
ure
(psi
)
17
16
15
14
13
12
11
Dis
pen
se P
ress
ure
(psi
)
17
16
15
14
13
12
11
300 kPa Dispense Maximum Pressure
250 kPa Dispense Maximum Pressure
0 100 200 300 400 500
Running Number
0 100 200 300 400 500
Running Number
0 100 200 300 400 500
Running Number
Top: Original air supply is at 350 kPa
Bottom: Original air supply is at 300 kPa
Top: Original air supply is at 250 kPa
Figure 6. Test results of Maximum Confirmation tool; Running No. 1 to 100: needle valve is fully opened, Running No. 101 to 200: Needle valve is ¼ closed, Running No. 201 to 300: Needle valve is ½ closed, Running No. 301 to 400: needle valve is ¾ closed and Running No. 401 to 500: needle valve is fully opened again.
6
Dis
pen
se P
ress
ure
(psi
)
350 kPa Dispense Average Pressure
5.5
5.0
4.5
4.0
3.5
3.0
7.0
6.5
6.0
5.5
5.0
4.5
4.0
3.5
6.0
5.5
5.0
4.5
4.0
3.5
3.0
Dis
pen
se P
ress
ure
(psi
)
Dis
pen
se P
ress
ure
(psi
)
300 kPa Dispense Average Pressure
250 kPa Dispense Average Pressure
0 100 200 300 400 500
Running Number
0 100 200 300 400 500
Running Number
0 100 200 300 400 500
Running Number
Top: Original air supply is at 350 kPa
Bottom: Original air supply is at 300 kPa
Top: Original air supply is at 250 kPa
Figure 7. Test results of Average Pressure Confirmation tool; Running No. 1 to 100: Needle valve is fully opened, Running No. 101 to 200: needle valve is ¼ closed, Running No. 201 to 300: Needle valve is ½ closed, Running No. 301 to 400: needle valve is ¾ closed and Running No. 401 to 500: needle valve is fully opened again.
Dis
pen
se P
ress
ure
Tim
e (s
ec)
350 kPa Dispense Maximum Pressure Time
1100
1050
1000
950
900
850
800
750
700
Dis
pen
se P
ress
ure
Tim
e (s
ec)
1100
1050
1000
950
900
850
800
750
700
Dis
pen
se P
ress
ure
Tim
e (s
ec)
1100
1050
1000
950
900
850
800
750
700
300 kPa Dispense Maximum Pressure Time
250 kPa Dispense Maximum Pressure Time
0 100 200 300 400 500
Running Number
0 100 200 300 400 500
Running Number
0 100 200 300 400 500
Running Number
Top: Original air supply is at 350 kPa
Bottom: Original air supply is at 300 kPa
Top: Original air supply is at 250 kPa
Figure 8. Test results of Maximum Pressure Time Confirmation tool; Running No. 1 to 100: needle valve is fully opened, Running No. 101 to 200: needle valve is ¼ closed, Running No. 201 to 300: needle valve is ½ closed, Running No. 301 to 400: needle valve is ¾ closed and Running No. 401 to 500: needle valve is fully opened again.
7
Pre
ssu
re (p
si)
350 KPa Reference Pressure Profile when Needle Valve is Fully Open
350 KPa Compare Reference Pressure Profile when Needle Valve is 1⁄4 Closed
16
14
12
10
8
6
4
2
0
Pre
ssu
re (p
si)
16
14
12
10
8
6
4
2
0
ReferenceNeedle valve
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
Pre
ssu
re (p
si)
350 KPa Compare Reference Pressure Profile when Needle Valve is 1⁄2 Closed
350 KPa Compare Reference Pressure Profile when Needle Valve is 3⁄4 Closed
16
14
12
10
8
6
4
2
0
Pre
ssu
re (p
si)
16
14
12
10
8
6
4
2
0
ReferenceNeedle valve
Reference
ReferenceNeedle valve
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
Figure 9. Pressure profile when original air supply is at 350 kPa.
Pre
ssu
re (p
si)
300 KPa Reference Pressure Profile when Needle Valve is Fully Open
300 KPa Compare Reference Pressure Profile when Needle Valve is 1⁄4 Closed
16
14
12
10
8
6
4
2
0
Pre
ssu
re (p
si)
16
14
12
10
8
6
4
2
0
ReferenceNeedle valve
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
Pre
ssu
re (p
si)
300 KPa Compare Reference Pressure Profile when Needle Valve is 1⁄2 Closed
300 KPa Compare Reference Pressure Profile when Needle Valve is 3⁄4 Closed
16
14
12
10
8
6
4
2
0
Pre
ssu
re (p
si)
18
16
14
12
10
8
6
4
2
0
ReferenceNeedle valve
Reference
ReferenceNeedle valve
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
Figure 10. Pressure profile when original air supply is at 300 kPa.
8
SUMMARY—Among the four pressure sensor based tools, the
Pressure Profile Compare showed the most sensi-
tive response when air supplied to the stop suckback
valve is weakened. The percentage of Pressure
Profile Compare test results drop to 80% from
100% of reference level when air supplied is half of
the original level, and 20% – 40% when air supply is
one quarter of the original level. Though the setting
limit for alarm activation depends upon the user,
in general the warning limit is usually set between
80% – 90% and the error limit is between 70% – 80%.
The 80% test result is sufficient to activate the alarm,
and the 20% – 40% test result is definitely able to
activate the alarm.
One can confidently use the Pressure Profile Com-
pare confirmation tool to accurately monitor air
supply fluctuations. Figure 12 shows the overall
dispense system setup.
Even though they are not the most responsive, the
Maximum Pressure, Average Pressure, and Maximum
Pressure Time pressure sensor based tools showed a
reliable response to this abnormal event. Test results
show an obvious and stable change when air supplied
to the stop suckback valve is weakened. These three
tools could also be used to monitor air supply
fluctuations.
Pre
ssu
re (p
si)
250 KPa Reference Pressure Profile when Needle Valve is Fully Open
250 KPa Compare Reference Pressure Profile when Needle Valve is 1⁄4 Closed
16
14
12
10
8
6
4
2
0
Pre
ssu
re (p
si)
16
14
12
10
8
6
4
2
0
ReferenceNeedle valve
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
Pre
ssu
re (p
si)
250 KPa Compare Reference Pressure Profile when Needle Valve is 1⁄2 Closed
250 KPa Compare Reference Pressure Profile when Needle Valve is 3⁄4 Closed
16
14
12
10
8
6
4
2
0
Pre
ssu
re (p
si)
18
16
14
12
10
8
6
4
2
0
ReferenceNeedle valve
Reference
ReferenceNeedle valve
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
-1.0 -0.5 0 0.5 1.0 1.5 2.0
Time (sec)
Figure 11. Pressure profile when original air supply is at 250 kPa.
9
SYSTEM LAYOUT—
CONCLUSION—Consistent air pressure is critical in maintaining high
quality control over chip manufacturing processes.
However, it is not easy to establish. Adding an air
pressure confirmation tool can help manufacturers
better control the wafer coating process. When the
ability to monitor and control air pressure increases,
wafer yield also increases.
Entegris has an innovative photochemical dispense
pump with an integrated pressure sensor. User-
friendly MMI software with robust confirmation tools
simplifies recipe programming and provides real-time
status. The integrated Pressure Profile Compare
confirmation tool is featured in the IG-Mini and new
pumps IG-ULV, IG-LV and IG-MV, and enables reliable
monitoring and control in numerous applications.
Implementing a dispense pump with a pressure
sensor confirmation tool can help minimize costly
wafer defects.
ACKNOWLEDGEMENT—The author would like to thank Entegris colleagues
Mitsutoshi Ogawa, application engineer, for engineer-
ing the test setup, Tomohiro Wagatsuma, field service
engineer, for participating in useful discussion, and
Keigo Yamamoto, product manager, for guiding the
experiment to completion.
Figure 12. Dispense system setup.
Drain
Inlet
OutletVent
Wafer
Nozzle
N₂ pressure
Bottle
L/E
Pump cable
Multi interface module
I/O signal
24V power
IntelliGen ULV/LV/MV
Outlet valve
Solenoid
IntelliGen NCS Factory database
Computer
Fluid
Utility
Electricity
N₂ pressureand vacuum
LAN
RS-422
Trackinterface
FOR MORE INFORMATION
Please call your Regional Customer Service Center today to learn what Entegris can do for you. Visit entegris.com and select the Contact Us link to find the customer service center nearest you.
TERMS AND CONDITIONS OF SALE
All purchases are subject to Entegris’ Terms and Conditions of Sale. To view and print this information, visit entegris.com and select the Terms & Conditions link in the footer.
www.entegris.com
129 Concord RoadBillerica, MA 01821 USA
Tel +1 952 556 4181Fax +1 952 556 8022Toll Free 800 394 4083
Corporate Headquarters Customer Service
Entegris®, the Entegris Rings Design®, and other product names are trademarks of Entegris, Inc. as listed on entegris.com/trademarks. All third-party product names, logos, and company names are trademarks or registered trademarks of their respective owners. Use of them does not imply any affiliation, sponsorship, or endorsement by the trademark owner.
©2018 Entegris, Inc. | All rights reserved. | Printed in the USA | 3811-10054ENT-0818