Ultrapure Gas Delivery
Devising specifications for optimizing point-of-use gas pressure regulators
Dan Morgan, Parker Hannifin Veriflo
A point-of-use pressure regulator must perform properly so that
it can provide steady gas pressure during delivery and maintain a consistent
set-point pressure when the gas stick is opened and closed.
Strides in computer performance and the decreasing cost of manufacturing
semiconductor wafers relative to size are the result of many small, incremental
improvements in wafer design and manufacturing processes. These improvements
rely, in turn, on the quality of all of the components that are used in
the fab, from the environmental system to the wafer processing tools themselves.
Therefore, advancements in the quality of such components, no matter how
small, are important to the entire semiconductor industry because they
either support or spawn other advancements. This article examines point-of-use
pressure regulators and the need to develop specifications that can optimize
their use and bolster the performance of the processing tools to which
they are attached.
Process Tool Gas Delivery System
One of the requirements of advanced wafer processing is that tool chambers
must receive a consistent, accurate, and repeatable supply of process
gases without perturbations or flow spikes that can affect the uniformity
of the wafer chemistry. Gas delivery subsystems, often referred to as
"gas sticks," fulfill this requirement. In a typical semiconductor fabrication
process line, gas sticks are used to initiate, deliver, and shut off the
flow of gases into process tools, as dictated by the process recipe. These
subsystems generally consist of several automatic shutoff valves, a pressure
regulator, and a mass-flow controller (MFC).
A gas stick receives its supply from a "gas room," which contains the
various high-pressure process gases used throughout the facility. These
gases are plumbed to a medium-pressure distribution manifold that moves
the gases from the lower-floor gas room up to the wafer-processing tools
located in the upper-floor cleanrooms. A given gas can be delivered to
several different tools and several chambers within each tool.
The gas stick incorporates valves that permit the inflow and outflow
of process gas and enable the stick to be purged of air prior to start-up.
The MFC is used to control the flow of gas to the tool chamber for the
duration of the process reaction. Because process steps can be as short
as several seconds in duration, it is important that the MFC ramp up from
zero to the desired flow as quickly as possible. The gas stick's point-of-use
regulator maintains a relatively constant pressure to the MFC inlet to
help stabilize flow. To ensure proper gas flow in the fab, it is useful
to understand how pressure regulators function and how they relate to
the MFC in a point-of-use gas delivery system.
Regulator Basics
A schematic diagram of a typical point-of-use regulator is presented
in Figure 1. This device controls pressure in a quite simple way. A handwheel
compresses a spring when turned. This spring, called a range spring, pushes
down on a metal diaphragm, which separates the process gas from the external
environment with a metal-to-metal seal. The diaphragm, in turn, drives
open the regulator poppet valve, which allows the high-pressure gas to
flow into the diaphragm cavity. When the gas pressure acting on the diaphragm
area generates a force equal to that of the range spring, the diaphragm
returns to a neutral position, allowing the poppet to close. The regulator
diaphragm maintains the balance between the range spring and the process
gas pressure. Several other forces within the regulator contribute to
this force balance, including the spring rate of the diaphragm itself
multiplied by the diaphragm stroke, the internal bias spring load, and
the inlet pressure acting on the poppet area. This force balance is mathematically
represented in the following equation:
(Pout x Adiaphragm)
+ Fdiaphragm + Fbias spring
+ (Pin x Apoppet)
= Frange spring
where
Pin is the regulator inlet pressure,
Pout is the outlet pressure (delivery pressure),
Adiaphragm is the diaphragm effective area,
Apoppet is the area of the poppet-to-seat seal,
Fdiaphragm is the upward force of the deflected
metal diaphragm,
Fbias spring is the force provided by the bias
spring, and
Frange spring is the force provided by the range
spring.
As the regulator opens to provide increasing gas flow, the poppet, diaphragm,
and springs move to create the required opening at the poppet and seat
interface for the set flow. While this "downward" repositioning of the
poppet results in a lower range-spring force because of reduced compression
on the range spring as the diaphragm moves downward, it also causes the
diaphragm and the bias spring to exert increased force. Consequently,
outlet pressure drops as flow increases. This relationship is shown in
Figure 2, a flow curve for a point-of-use regulator that depicts the change
in outlet pressure as a function of flow. The flow curve illustrated in
Figure 2 is actually composed of two curves, each of which represents
regulator outlet pressure at any given flow rate, as flow is increased
and then decreased. The measured pressure difference between these two
curves at any point is the hysteresis of the regulator. Hysteresis is
caused by friction between the regulator components. Many regulator designs
incorporate a friction device that helps to dampen the runaway oscillation
which occurs in an underdampened pressure regulator. The steep slope at
the beginning and termination of flow is described as the "creep" or "lockup"
region of the flow curve.
 |
| Figure 1: Schematic diagram of a typical point-of-use gas regulator.
|
 |
| Figure 2: Example of a typical flow curve showing regulator outlet
pressure as a function of gas flow. |
Under steady-state flow conditions, the regulator maintains a force
balance between the regulator outlet pressure applied to the diaphragm
and the regulator range spring, while negligible force is exerted on the
regulator poppet and seat interface. When flow is terminated, outlet pressure
continues to rise until sufficient force develops between the poppet and
seat to effect a seal.
When flow is initiated through the regulator, the creep pressure is
drained off before the regulator poppet lifts off the seat. If there is
any appreciable friction between the poppet and the seat, the outlet pressure
continues to drop slightly below the outlet pressure set point before
jumping back up when the static friction has been overcome. Referred to
as transient overshoot, this sudden reversal in the slope of the regulator
outlet pressure relative to time can cause the MFC to spike. The timing
of this event can be critical to the process and is dependent on system
volume, flow rate, and the amount of creep pressure buildup.
The response of a regulator relative to time as a change in the flow
rate occurs, known as transient response, is an important aspect
of regulator performance. While any change in flow rate affects regulator
outlet pressure, the change from zero flow to a low-flow setting has the
greatest impact on semiconductor processes. Low-flow transient response
is illustrated in Figure 3, which presents a graph of regulator outlet
pressure as a function of time as flow is initiated in a regulator exhibiting
excessive friction. This graph shows that the outlet pressure of this
regulator overshot the desired pressure set point by 1.0 psi.
 |
| Figure 3: Low-flow transient response test showing the response
of a regulator's outlet pressure as flow changes quickly from 0 to
350 std cm3/min. Transient overshoot is 1.0 psi. |
Testing Regulator Performance
A series of tests was performed to investigate the relationship between
regulator performance and the stability of gas delivery from a point-of-use
gas delivery system under the flow-rate conditions that are typical in
semiconductor fabrication processes. A schematic of the gas delivery system
used to perform the tests is illustrated in Figure 4. The system consisted
of a system inlet pressure transducer, a pressure regulator, a regulator
outlet pressure transducer, an air-operated isolation valve, a mass-flow
controller inlet pressure transducer, a mass-flow controller, and an air-operated
outlet valve. The system's inlet pressure was set at 65 psia while the
regulator outlet pressure was set at 30 psia at zero flow. The flow settings
of 20 and 100 std cm3/min were 20 and 100% of full MFC scale.
Control signals to the air-operated valves and the MFC were given simultaneously.
To maintain consistency relative to the MFC in-line leak rate, the system
was opened and then closed for 10 seconds before each test was begun.
 |
| Figure 4: Schematic of a high-purity point-of-use gas delivery
system incorporating (a) a regulator inlet pressure transducer, (b)
a pressure regulator, (c) a regulator outlet pressure transducer,
(d) an air-operated valve, (e) an MFC inlet pressure transducer, (f)
an MFC, and (g) an air-operated outlet valve. |
The effect of regulator friction on pressure stability was studied in
a step function transient response test. As described in Semaspec Standard
90120392B-STD ("Test Method for Determination of Regulator Performance
for Gas Distribution System"), this test demonstrates the effect of friction
on regulator outlet pressure as gas flow is quickly changed from 25 to
50% of the maximum rated flow for the regulator. The maximum rated flow
is defined as the maximum flow within the regulator's control range, or
the maximum flow recommended by the manufacturer. A test using the maximum
flow within the control range of a state-of-the art point-of-use regulator
provided the following values:
- Test regulator inlet pressure = 50 psig.
- Test regulator outlet pressure = 15 psig.
- Maximum rated flow = 50 std L/min.
- 25% maximum rated flow = 12.5 std L/min.
- 50% maximum rated flow = 25 std L/min.
Because most semiconductor fabrication facilities use flow rates that
are far lower than the test flows provided by this method and, as this
study demonstrated, the step function transient response test does not
provide an adequate measure of pressure stability in typical low-flow
applications, a low-flow transient response test was explored to evaluate
regulator response to a sudden initial demand for flow. This low-flow
transient response test differs from the SEMI transient response test
in Semaspec 90120392B-STD because regulator response is evaluated as the
flow rate is varied quickly from 0 to 350 std cm3/min. Data
were collected at a rate of 1000 samples per second using Labview data
acquisition software (National Instruments, Austin, TX).
Three regulators displaying widely varying low-flow transient response
behavior were tested. The Semaspec method was used to test these components
for step function transient response. The test data were then analyzed
to determine whether there was a quantifiable difference between the regulators.
Finally, the regulators were installed in the type of gas-flow system
that is typically used in semiconductor fabs and tested to determine the
effects of the varying degrees of low-flow transient response.
In test 1, regulator outlet pressure and gas flow were measured as a
function of time as flow was initiated. The test flow rate was 20 std
cm3/min and the MFC was set at 20% of full flow capacity. In
test 2, the flow rate was 100 std cm3/min and the MFC was set
at 100% of full flow capacity while the other parameters remained the
same. Tests 3 and 4 were the same as tests 1 and 2, respectively, except
the pressure across the MFC was allowed to equalize to demonstrate the
effects of a relatively long delay before the initiation of gas flow.
A range of parameters related to the operation of the components shown
in Figure 4 were monitored as a function of time: system inlet pressure
(a), regulator outlet pressure (c), the pressure-control signal to the
air-operated valves (d and g), the control signal to the MFC (f), MFC
inlet pressure (e), and the MFC flow rate. The test data were analyzed
to determine regulator transient overshoot, transient response, regulator
stabilization time, MFC stabilization time, and flow spike as a percentage
of set flow (only spikes that occurred after the MFC had stabilized are
reported). Values for these parameters are presented in Tables I and II.
|
Test Flow
|
Regulator Transient Overshoot
(psi)
|
|
Regulator 1
|
Regulator 2
|
Regulator 3
|
|
20 std cm3/min
|
0.10
|
0.50
|
1.0
|
|
100 std cm3/min
|
0.10
|
0.50
|
1.0
|
|
| Table I: Transient overshoot values for three test regulators.
|
|
Regulator
|
Regulator
Transient
Response (psi)
|
Regulator
Stabilization
Time (sec)
|
MFC
Stabilization
Time (sec)
|
Flow Spike
(% of
set flow)
|
| Test 1: 20 std
cm3/sec Flow Rate |
| 1 |
0.1 |
4.0 |
0.9 |
0 |
| 2 |
0.5 |
2.5 |
0.9 |
0 |
| 3 |
1.0 |
3.0 |
0.9 |
0 |
| Test 2: 100 std cm3/sec
Flow Rate |
| 1 |
0.1 |
1.0 |
0.6 |
2.0 |
| 2 |
0.5 |
1.0 |
0.6 |
4.0 |
| 3 |
1.0 |
1.7 |
0.6 |
9.0 |
| Test 3: 20 std
cm3/sec Flow Rate (Pressure Equalized across MFC)
|
| 1 |
0.1 |
1.0 |
1.3 |
0 |
| 2 |
0.5 |
2.5 |
1.3 |
0 |
| 3 |
1.0 |
3.6 |
1.4 |
0 |
| Test 4: 100
std cm3/sec Flow Rate (Pressure Equalized across
MFC) |
| 1 |
0.1 |
1.0 |
0.6 |
0 |
| 2 |
0.5 |
0.6 |
0.6 |
0 |
| 3 |
1.0 |
0.7 |
0.6 |
0 |
|
| Table II: Results of low-flow transient response tests. |
In all the tests, flow spikes were initially registered as the isolation
valve (d) was opened. These spikes, a product of the MFC design, were
caused not by flow but by voltage. They were most severe when the pressure
across the MFC was equalized before flow was initiated. As depicted in
Figure 5, the rush of pressure into the MFC caused it to close, delaying
the flow of gas.
 |
| Figure 5: MFC flow relative to regulator performance. |
The data for regulator 3, test 2, illustrated in Figure 6, revealed
that a regulator outlet pressure transient overshoot of 1.0 psi is sufficient
to cause an MFC to react, giving a flow signal in excess of 5% of the
flow set point. Consequently, a maximum transient overshoot specification
of 0.5 psi for regulator transient response is required to provide adequate
pressure stability and ensure stable gas delivery.
 |
| Figure 6: MFC flow relative to regulator performance showing
degree of overshoot. Graph of regulator outlet pressure as a function
of time at onset of gas flow shows that the outlet pressure of the
regulator overshot the desired pressure set point by 1.0 psi. |
Conclusion
The low-flow transient response test described in this article can quantify
the performance of a regulator at the start of gas delivery. This test
enables process engineers to qualify a regulator for point-of-use semiconductor
applications.
In order to ensure adequate pressure stability and guarantee that the
MFC used in these tests provided stable gas delivery, the regulator transient
response overshoot specification could not exceed 0.5 psi. However, different
MFCs‹even from the same manufacturer‹display varying levels of sensitivity
to transient overshoot. Advances in regulator response must keep pace
with faster-opening MFCs so that a fast-acting, stable gas delivery system
can be established.
By understanding the interaction of the various components used in a
gas stick, the requirements for each component can be specified, ensuring
that semiconductor manufacturers have access to the best possible gas
delivery system.
Acknowledgments
The author would like to thank Warner Thelan, a test engineer at Parker
Hannifin's Veriflo division in Richmond, CA, whose expertise in testing
pressure regulators contributed to the substance of this article, and
to Bill Stubbs, an applications engineer at Veriflo, who contributed to
the article's development aspect.
Dan Morgan is the research and development manager at Parker
Hannifin's Veriflo division in Richmond, CA. He joined the company (formerly
called Veriflo Corp.) in 1984 as a manufacturing engineer before being
promoted to the position of design engineer. Morgan is an expert in high-purity
regulator design for the semiconductor industry, an area in which he holds
two patents. He received a BS in mechanical engineering from Washington
State University in Pullman, WA. (Morgan can be reached at 510/412-1253
or danmorgan@veriflo.com.)

MicroHome |
Search | Current Issue | MicroArchives
Buyers Guide | Media Kit
Questions/comments about MICRO Magazine? E-mail us at cheynman@gmail.com.
© 2007 Tom Cheyney
All rights reserved.
|