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Desi=
gn and
Development of a Sub-Scale
Monopropellant Gas Generator
Kevin Lohner, Jonny=
Dyer,
Eric Doran, Zachary Dunn,
Valentin Decker, Er=
ic
Wooley, and Andy Sadhwani
Stanford Uni=
versity,
Stanford, CA, 94305, USA
Professor Thomas Ke=
nny
Stanford University, Stanford, CA, 94305, USA
Research Sponsored =
in part
from:
=
o:p>

Pratt & Whitney Rocketdyne, Canoga Park, CA,
91309, USA
Abstract
=
There is renewed
interest within academia, industry and government agencies in storable,
non-toxic propellants for a variety of aerospace applications. Of particular interest – due=
to
its simplicity, low-cost, and safety – is a catalytic gas generator d=
evice
capable of decomposing monopropellants such as nitrous oxide and/or very le=
an
nitrous oxide / fuel mixtures.
=
=
A monopropellant
is a single fluid capable of undergoing exothermic reaction to yield a gase=
ous
product, commonly through a decomposition process. In a monopropellant gas generator
system, only a single tank and propellant feed system is required. Injection is simplified as there i=
s no
mixing required. Because of t=
hese
reasons operations are simpler in the field and on-orbit.=
=
=

=
=
Preliminary
studies have indicated that scaling such a device down to the meso- or
micro-scale could enable benefits in thrust-to-weight, start-up transients,
cost, and robustness, while still yielding a high level of performance. Using an innovative micro-fabricati=
on
approach, this device could enable production economies of scale. The modular design allows for its =
use in
a wide range of propulsion and power applications, such as:
=

It is most desirable for =
monopropellants
to have the following qualities:
- Non-toxic
- High liquid density
- High specific impulse
- High characteristic exhaust velocity
- Stable long-term storage
- Low cost
As nitrous oxide is a ver=
y worthy
candidate, the lab-scale N2O test facility at Stanford Universit=
y (Figure 1), modified with a catalyst bed test article assem=
bly
(Figure 2), is being used for preliminary testing. Initial results have proven the co=
ncept
to be valid.

Figure 1: Stanford
Lab-Scale Nitrous Oxide Test Facility
=
p>
=

Figure 2: =
Basic Test Set-up for
Lab-Scale Monopropellant Gas Generator
=
Making
this device on the micro scale is the key aspect to making a successful N2O
catalyst. Historically, the m=
ain disadvantages in making a nitrous =
oxide
gas generator on the large, macro=
i>
scale are:
=
p>
·
High cost of
catalyst materials (iridium, rhodium, platinum, Shell 405) needed for a lar=
ge
size gas generator.
·
Difficulty =
in the
long-term integrity of the catalyst (and support structure) due to 1640°=
;C
decomposition temperature, and no good way of actively cooling the catalyst
substrate. This drives the us=
e of a
pelletized bed, which over time cracks, crumble=
s, and
can become poisoned.
·
Low
Thrust-to-Weight (T/W) ratio (compared to hydrazine catalyst gas generators)
due to lower specific impulse of N2O decomposition and high structural mass
fraction for the catalyst and refractory metal chamber walls (needed due to
1640°C hot gas).
·
Practicalit=
y of
preheating the high volume of incoming gas flow to the 200°C necessary =
to
initiate the catalytic decomposition.
·
Slow start-=
up
transients due to large volumes of structure and fluid (high thermal
capacitance) that need to be pre-heated and activated before reaction reaches steady-state.=
The slow reaction kinetics require a very=
bulky
and long-length catalyst bed to get sufficient residence time.=
span>
=
p>
=
However,
making a micro-scale nitrous oxide catalyst gas generator can solve many of
these issues. The following s=
ix
items address these design features:
=
p>
·
Micro-fabri=
cation
enables a high-production-rate, low-cost, batch process using silicon and
silicon carbide as structural materials.&n=
bsp;
Deep Reactive Ion Etching (DRIE), wafer bonding, and Chemical Vapor
Deposition (CVD) can be used to create these high aspect ratio structures.<=
span
style=3D'mso-spacerun:yes'> These materials are relatively
inexpensive on a per-device basis.
Additionally, at the micro-scale, the higher surface-area-to-volume
ratio means less of the expensive noble metal catalyst needs to be used,
drastically reducing cost. Ph=
ysical
Vapor Deposition (PVD) of thin films of metals such as iridium, rhodium, and
platinum is routinely performed.
=
p>
·
The high su=
rface
area-to-volume at the micro-scale makes actively-cooling the structure and
catalyst substrate a more feasible and effective task. Silicon and silicon carbide have a
relatively good thermal conductivity, and cooling passages can easily be et=
ched
just behind the hot gas walls and even within the catalyst substrate.<=
/o:p>
=
p>
·
The light-w=
eight,
high-specific-strength structural materials (Si=
, SiC, and Al2O3) which are used =
for
fabrication enable significant weight savings over larger devices that use
metal construction. These
monolithic ceramics can not be used on large-scale devices due to the
stochastic presence of cracks or defects above the ‘critical flaw
size’, which drastically reduce the fracture toughness. However on the micro-scale, these
materials are near flawless, and their strength can approach theoretical
values. This is the same mech=
anism
that explains why carbon fibers and glass fibers have such high strength.
=
p>
·
The
‘Cube-Square Law’ also enables significant weight savings on the
micro-scale. Thrust is propor=
tional
to the cross-sectional area of the flowpath (F =
=3D Cf ∙ Pc ∙ At), or the ‘square’ of the len=
gth
dimension; whereas weight is proportional to the volume of the device, or t=
he
‘cube’ of the length dimension. Therefore, when scaling down to a
micron-sized device, weight decreases at a much faster rate than does
thrust. This fact, along with=
the
use of high-specific-strength materials, makes for relatively high T/W ratio
devices.
=
p>
·
The small
dimension of the incoming nitrous oxide flowpath
combined with the high surface area-to-volume make heating the fluid to 200=
°C
by way of embedded electrical resistors a very practical and feasible
approach. The use of a regeneratively-cooled system can aid in speeding up t=
he
pre-heat process to initiate the catalytic decomposition, making it more
efficient as well. Once self-=
sustaining
nitrous decomposition is achieved, the electrical power input is no longer
required.
=
p>
·
On the
micro-scale, the feed system can be more close-coupled to the device, requi=
ring
significantly less priming time. The overall result would be a faster start=
-up
transient.
=
p>
=
One of the
only main disadvantages to decreasing to this size scale is that viscous lo=
sses
now may be more dominant in the low Reynolds number flow regime. From a flow mechanics standpoint, =
the
design of the micro catalyst structure and the injector is also critical. A research program at Stanford
University has been initiated to analyze, numerically model, and experiment=
ally
demonstrate an effective nitrous oxide catalytic gas generator. Work will be performed to analytic=
ally
determine limits such as minimum pre-heat required and maximum bed loading.=
The proposed methodology =
to
developing the final device is two-part.&n=
bsp;
First, a workhorse, proof-of-concept device will be fabricated to te=
st
out the mechanisms and theory behind the device. It will be built as small as possi=
ble in
an attempt to match the Reynolds number and heat transfer regime of the tar=
get
device, yet large enough such that conventional machining methods and mater=
ials
can be used – keeping costs to a minimum. The
effectiveness of the following catalysts shall be determined: traditional catalysts (such as She=
ll
405, platinum, and palladium) and mixed metal oxide catalysts. A notional design of such a=
meso-scale device (nominally 1 inch
diameter by 2 inches long) is shown below in Figure 4

Figure 4: Notional
Illustration of Meso-scale Monopropellant Catalytic Gas Generator
Goals for the research include:
- Determining
minimal preheat temperature requirement for different catalyst /
propellant combinations
- Minimizing
thermal capacitance of the system to enable fast start-up transients=
li>
- Determining
optimal catalyst bed length while minimizing pressure drop and amount =
of
catalytic material required
- Maximizing
the bed loading parameter for different catalyst / propellant combinat=
ions
- Maximizing
c* efficiency of reaction
- Maximizing
exhaust gas temperature for application as an igniter or hot gas gener=
ator
Based on the findings in =
the
proof-of-concept device testing, a path for fabricating a micro-sized catal=
ytic
gas generator will be determined.
This could either be though selective laser sintering fabrication
methods, or by multi-wafer stack MEMS fabrication methods. The micro-scale device should show=
a
path to achieve all of the benefits described earlier in this proposal (low
cost, long life, high thrust-to-weight, low power consumption, and fast
start-up transient). Some of =
the
foreseen challenges for such a device include thermal management, low c* ef=
ficiency
due to incomplete decomposition, and joining issues complicated by mismatch=
in
thermal expansion coefficients of the materials involved.
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