Microgravity Science Glovebox / ISS Research Program
Shear
History Extensional Rheology Experiment II (SHERE II)
Astronaut Mike Fossum With SHERE
Flight Engineer Mike Fossum aboard the International Space Station takes a moment
to demonstrate the Shear History Extensional Rheology Experiment. Known as SHERE,
the experiment investigates the effect of rotation on the stress and strain response
of a polymer fluid being stretched in microgravity. SHERE provides information
that is critical for the evolution of containerless processing, an important
operation for fabrication of parts used on future exploration missions.
SHERE II status
May 22, 2012 - The SHERE main hardware (Rheometer, Interface
Box, Tool Box, Cables & Keyboard) along the SHERE II fluid modules
and stowage tray are scheduled to come down from ISS on the Space-X
Demo flight which successfully launch on May 22, 2012.
SHERE II Operations are complete!
Aug 24, 2011 - SHERE II was removed from the Microgravity Science Glovebox
and the hardware was stowed.
Aug 20, 2011 - Astronaut Mike Fossum completed the last ten test runs
setting a new record for the number of test runs done at one time.
Aug 16, 2011 - Astronaut
Satoshi Furakawa completed three sets of science test runs.
Aug 15, 2011 - Astronaut Satoshi Furakawa completed three
sets of science test runs.
Aug 11, 2011 - Astronaut Mike Fossum did his planned three test points
and then proceeded to do four additional test points within the original allotted
time. This
amazing accomplishment is an indication of the efficiencies gained by continuous
crew operation of the SHERE hardware.
Aug 10, 2011 - Astronaut Satoshi Furakawa performed the Dry Run
which is used to verify SHERE hardware operation and to serve as a final practice
session for him before he begin science operations .
Aug 8, 2011 - Astronaut Mike Fossum completed the first two sets of
science test runs.
Aug 3, 2011 - Mike performed the Dry Run which is used to verify SHERE
hardware operation and to serve as a final practice session before science operations
begins on the 25 fluid modules.
Aug 2, 2011 - Astronaut Mike Fossum successfully completed the rest of the
checkout test.
July 25, 2011 - Check-out of several hardware components was started
today but had to be cut short following an anomaly with the flight software.
After 2 days of troubleshooting, the software was corrected and re-verified and
sent to MSFC to be uploaded to the Microgravity Science Glovebox laptop computer.
June 30, 2011 - Astronaut Satoshi Furakawa successfully installed the SHERE
hardware (Interface Box, Rheometer, Camera Arm, Keyboard, Toolbox and cable assemblies)
in the Microgravity Science Glovebox.
May 16, 2011 - The Fluid Modules (consisting of 25 filled Fluid Modules
and one "dry" Fluid Module) were launched on the STS 134 Endeavour
(Flight ULF-6). Ironically, astronaut Greg Chamitoff and Mike Fincke who operated
SHERE during Increment 17 and 18 respectively, were on the shuttle mission that
carried the SHERE fluid modules to ISS.
March 2011 - SHERE
II successfully passed its Executive Systems Acceptance Review and
received approval to ship the flight hardware from Glenn in preparation
for flight on STS-134 (ULF6 Middeck).
May 2010 - The Shear
History Extensional Rheology Experiment II (SHERE II) flight experiment
completed its Engineering Systems Acceptance Review-1 on May 12,
2010. This purpose of the review was to obtain engineering
board assessment on the acceptability of the SHERE II hardware to
proceed with shipment for flight STS-134 (ULF6 Middeck). The
hardware scope of the review was the reflight of the Fluid Modules
and Fluid Module Stowage Tray as the main hardware is already in
orbit on ISS.
Following the successful completion of the SHERE
Increment 18 operations, the newly redesigned 25 FM was returned to
earth. These Fluid Modules will be emptied, cleaned and inspected.
This will allow them to be refilled to permit reflight and re-use
of the extensional rheometer that is currently in storage aboard ISS.
The natural next step is to use the SHERE hardware
to probe the extensional rheology of a different non-Newtonian fluid.
In principle this is straightforward, however stringent ISS safety
requirements would require ground based testing of seal compatibility,
sample cleanup, offgassing if a completely new fluid was selected.
However, we propose a much simpler approach: we seek to extend our
knowledge by augmenting the existing polystyrene flight fluid with
a dilute concentration (5%) of rigid inert filler.
Filled polymeric suspensions form the bulk of the
engineering plastic market; by replacing a fraction of the (relatively
expensive) synthetic polymer in a plastic product with a cheap mineral
filler (e.g. titania (TiO2), silica (SiO2) or carbon black) it is
possible to lower the cost, and enhance properties such as environmental
sensitivity to UV degradation, water-swelling etc. However, as we
describe in detail below, the systematic understanding of such fluids
is in its infancy because of the nonlinear interactions between the
matrix viscoelasticity and the rigid filler. The no-slip boundary
condition on the surface of the filler results in additional shear
stresses, in all processing flows and enhances the total viscoelasticity.
In the past four years, theoretical advances have led to a proper
asymptotic constitutive theory for dilute suspensions of rigid spherical
fillers dispersed in dilute polymer solutions [3,4]. This theory was
validated in shear by comparison with ground-based shear rheology
experiments performed in the P.I.’s lab [10], and makes explicit
predictions (See Eq. (1) below) of the change in the extensional viscosity
induced by the additional shearing kinematics induced by the rigid
particles. The SHERE rheometer provides a perfect platform for testing
this new theory because of the ability to independently control the
shear rate and the extension rate in the rheometer.
We thus propose to formulate an enhanced fluid consisting
of a dilute suspension (5 vol%) of rigid inert polymethylmethacrylate
(PMMA or ‘Plexiglas’) microspheres (diameter d =
6 or 15 µm) dispersed in the same Polystyrene Boger fluid used
for Increment 17 and 18 (consisting of a dilute solution (0.025 wt.%)
of a narrow polydispersity high molecular weight polystyrene dissolved
in oligomeric styrene oil). The specific formulation is discussed
in the next section; however it is important to note that this fluid
can be rapidly formulated and readily characterized on the ground
in the P.I.’s laboratory because (i) an excess of base fluid
was originally formulated for the SHERE experiments, and (ii) the
inert filler (spherical plexiglass beads) are also already available
in the P.I.’s laboratory. The base fluid that has been stored
in cold dark conditions will comprise 95% of the new test fluid and
is ready to use immediately.
We propose to clean and fill the 25 FM that have
been returned following Increment 18 with this new test fluid. Because
the rheometer hardware is already in orbit, it is only necessary to
launch new fluid samples, and the resulting upmass is minimal. The
redesigned fluid modules used in Increment 18 performed flawlessly
and there is no necessary additional redesign work for the hardware
or the fluid modules. The new design enables a better deployment of
the fluid column using a new chamfered lip design that prevents the
fluid from wetting the force transducer endplate. As a result, a nice
cylindrical fluid column pinned at the edges of the transducer plate
is obtained, which guarantees well-defined initial conditions for
subsequent numerical modeling. The only ground-based testing required
before reflight will be a deployment test to ensure that the dilute
concentration of inert microspheres do not interfere with the performance
of the seals.
Theoretical Background and Objectives
SEM image of PMMA rigid microspheres of diameter 15 µm (courtesy
of Dr. Anne Kari Nyhus from Microbeads AS).
The goal of the SHERE II experiment will be to investigate
the effects of a pre-shear history on the transient extensional viscosity
in a uniaxial stretching flow for a model filled viscoelastic suspension
(consisting of inert rigid non-Brownian spheres dispersed in a dilute
polymer solution). The role of internal stresses produced by shearing
between the rigid filler and the viscoelastic matrix can be explored
systematically using the pre-shear capabilities of the SHERE platform.
Access to extended microgravity also allows the subsequent relaxation
behavior to be measured after cessation of the extensional deformation
during the extended range of time scales that can be accessed because
of the absence of gravitational sagging. As with the original SHERE
experiment, SHERE II will be operated inside the Microgravity Science
Glovebox (MSG) aboard the International Space Station (ISS).
Rapid Turn-Around: The major
advantage of the proposed SHERE II experiment is that it will only
require us to clean and refill the existing (redesigned) 25 fluid
modules from Increment 18 once they have been returned to earth. No
additional engineering and optimization will be required for these
fluid modules that already proved their performance during Increment
18.
Numerical distribution of shear rate for a suspension of hard particles
in planar elongational flow.
In addition, the base fluid (or ‘matrix fluid’ in
the language of suspension mechanics) will remain unchanged, namely
a dilute solution (0.025 wt.%) of a narrow polydispersity high molecular
weight polystyrene dissolved in oligomeric styrene oil. This fluid
has already been fully characterized in our lab and sufficient fluid
remains to form the matrix fluid for the proposed SHERE II test matrix.
The ISS experiments already performed without suspended microspheres
correspond to a particle volume fraction f = 0 and thus
serve as a reference or baseline; these tests will not have to be
repeated for SHERE II. This is another benefit of using the same base
Boger fluid.
Footprint on powdery lunar regolith taken during Apollo 11 mission.
Also, the hard microspheres of diameter 15 µm
that will be used as filler particles do not have to be synthesized
from scratch but are now readily commercially available under the
brand name “spheromer” [3] from Microbeads SA (http://www.micro-beads.com).
A range of sizes are available from 1 – 50 µm. The smallest
sizes d ≤ 1 µm cannot be used because the existing
theory is for non-Brownian spheres (ie Brownian motion is negligible);
the larger sizes are increasing prone to sedimentation effects (under
1 g) which become worse as ~ d2. These sedimentation effects
can be mitigated using an available rotisserie system, but preliminary
calculations show they can also be designed to be of minimal importance
by reducing the particle size to d = 6 or 15 µm. A
SEM image of the 15 µm microbeads is shown in Fig. 2 (c). According
to the supplier, the bead size distribution is very narrow and the
microspheres are almost monodisperse, which is suitable for subsequent
numerical modeling.
SEM image of an individual grain of lunar regolith (Source: NASA).
Understanding the rheological properties of highly
viscoelastic suspensions may be of paramount importance for lunar
in-situ resource utilization and for the future construction of a
permanent lunar base. Indeed, the lunar soil, referred to as regolith,
is composed of loose dust and broken rocks as shown in Fig. 3 that
could be used as a high volume fraction filler when mixed with a polymeric
binder or matrix for building foundation or roadbed materials. The
viscoelastic dilute suspension used for SHERE II thus serves as a
highly idealized model system amenable to theoretical analysis which
can shed light on future development of lunar regolith-based construction
materials.
Suspensions of particles in viscoelastic liquids
are used in many earth processing operations: polymer melts with fillers,
ceramic pastes, biomedical materials, food, cosmetics or detergents.
The final properties of the suspensions are greatly determined by
the shape, concentration and size of the filler. In particular, the
fillers can range from nanoscopic to microscopic characteristic dimensions,
which leads to very different types of flow behaviors, filler/matrix
interactions and dynamics.
Relevance to NASA Research Mission
The SHERE II experiment will allow us to measure,
for the first time, the transient extensional viscosity in a uniaxial
stretching flow for dilute polymer suspensions. In addition, SHERE
II will enable us to study the subsequent fluid relaxation behavior
after cessation of the extensional deformation, which is not possible
in a 1-g environment because of sagging issues [13]. This research
has direct applications in many industrial processes involving filled
viscoelastic systems, ceramic pastes, biomedical materials, food,
cosmetics or detergents.
Secondly, as noted above, the possibility of
using lunar regolith as high volume fraction filler when mixed with
a polymeric binder or matrix has application for future lunar exploration;
e.g. the regolith may be blended with a viscoelastic binder (e.g.
bitumen or other resin-like binder) for augmenting the volume and
compressive strength of building foundation or roadbed materials. We
have recently become aware of a regolith simulant (JSC-1A)
that could also be used in future rheometric investigations. The
additional rheological challenges associated with this material
relate to the broad polydispersity of sizes and the high aspect
ratio/angularity of the filler. In parallel with preparation of
the SHERE II flight fluid (0.025wt%PS/5% PMMA spheres/94.975% oligomer),
the PI will also begin ground-based experiments using a viscoelastic
regolith suspension.
Principal Investigator: Prof.
Gareth McKinley, MIT gareth@mit.edu
Contacts at NASA Glenn Research Center Project Manager/Project
Scientist: Nancy R. Hall, NASA GRC Nancy.R.Hall@nasa.gov 216-433-5643