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EXPERIMENTS |
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1. Methanation in a fixed bed catalytic reactor CatReact TA: Torren Carlson This experiment studies the
nickel catalyzed methanation from CO and H2. The catalyst can easily
deactivate due to the formation of coke on the Ni. This occurs when CO is
added in excess of stoichiometric. H2 at ca. 300C for several
hours activates the catalyst and reverses coke formation. This semester we have two reactors in
place, a CSTR and a PFR. The general kinetics (L-H kinetics), including
activation energies for the rate controlling step, the regions for diffusion
control, and catalyst deactivation (and regeneration) can be studied. We have
a new surface analyzer (a single point BET system) in the lab by which you
can measure the surface areas for the catalyst and thus to estimate a TOF,
turn over frequency. There are several kinetic simulation packages for
catalytic reactions that may be employed to represent the catalytic reactors. 2. Polymerization kinetics PolyKin TA: Vikram Daga Methyl-Methacrylate is
polymerized with AIBN as the initiator in this batch polymerization in a
dilatometer. The polymerization can be run in several ways: bulk, or in
toluene, butanol, methanol, benzene and/or cyclohexane. In all cases, you are
to focus on the differences between the results you find and those of prior
studies in our labs or in the literature. In the case of literature results,
you will most probably confirm their findings. Differences in the kinetics
should be studied; specifically, the activation energies will differ for
certain optional changes. In other cases, the differences will be most
reflected in the nature of the polymer product that is produced. For polymer
products, the first measure is the molecular weight distribution, which will
be measured with GPC in the PSE department (you will need to understand the
technique). We will work a protocol whereby this characterization data can be
obtained for a limited number of samples (e.g., < 6 in two sets of four).
You should be familiar with those kinetic and mechanistic components that
control the molecular weight distribution.
These experiments are typical in the development of a new polymer product(s)
wherein the range of reaction variables are studied to optimize a polymer for
specific applications based on the polymer properties, MWD being the first. 3. Binary Distillation Distill TA: Sumeet Pandey The purpose of this experiment
is to introduce you to elementary aspects of the most widespread separation
technique in the chemical industry – distillation. The assignments
allow the important concepts of reflux and reboil to be demonstrated, and to
examine how these variables influence the purity of the distillate and
bottoms streams. Because the column is fitted with view ports on many trays,
hydrodynamic effects such as flooding and weeping can also be observed. The primary control
variables are the steam into the reboiler and the reflux flow. The dependant
variables are the bottom and product compositions, respectively. Several
variables dictate the dynamics and eventual control of product compositions.
It is crucial that you present a proper energy analysis of this system. There
are several options in the analysis of energy, depending on where you draw
the boundaries. All involve measuring the rate of steam condensing in the
reboiler. We will have a sight glass to monitor the level of liquid at the
exit of the reboiler and you will need to work out a protocol to quantify the
energy transferred from the steam. 4. BioDiesel BioDiesel TA: Torren
Carlson The production of BioDiesel
is one of the fastest growing processes to produce liquid fuels from
renewable resources. Vegetable oils, fats and algae extracts are converted to
Diesel fuels for use in home heating, Diesel engines and turbines (including
jets and generators). The basic reaction is a trans-esterification process
that converts the triglycerides of oil to FAMEs (look it up) by the base
catalyzed reaction with methanol (or ethanol). However, current processes and
plants are far from optimum. You will study the kinetics of these reaction and associated separation processes with
the goal of understanding the opportunities for process improvement in
BioDiesel plants from raw or waste vegetable oil. 5. Characterization/Control of a heat exchanger HeatEx
TA: Sumeet Pandey The focus for this semester
is heat exchange. One is first to estimate the various heat transfer
coefficients for the system at the several interfaces in this system (inner
and outer) and the changes that occur as a function of the various flows
(water and steam). You should complete an energy balance on the system for
different configurations. These options involve control of any of several
temperatures (of the process or cooling water at various points) employing
any of several variables (steam, cooling and process water). The process can
be operated in co- or counter-current flow modes for the water-water heat
exchanger. What are the differences? 6. Membrane separation by
permeation The permeation experiments
studies the enrichment of oxygen from binary and tertiary gas mixtures
flowing in series or/in parallel into two permeation bundles. You can
investigated separation of O2 from N2, Ar and He. You
will have mixtures of O2 in He, N2 and Ar and O2
in CO2 as well as ternary mixtures of N2/O2/CO2
and N2/Ar/CO2, often with different mole fractions. You
will propose to compare the enrichment of oxygen as a function of
flow-rate/back-pressure from different feeds and to compare these to prior
separations (employing different feed compositions). 7. Ion exchange IonEx TA:
Soumitra Choudhary 'Sam' The Ion exchange experiments
will compare a variety of ion-exchange resins for the removal of Copper
Sulfate from an aqueous solution. There will be four new resins available,
all strong acid cation resins produced by Dow. These represent different
particle sizes for the same resin. Another represents a different degree of
cross-linking. And, finally, there is a product called, “ 8. pH Reactor Control pHControl
TA: Sumeet Pandey This experiment involves the
control of a liquid-phase reactor to neutralize acid-base streams. As in all
control situations, the initial approach is to understand and analyze the
reactor dynamics followed by the design and implementation of a control
scheme. A buffer stream can also be introduced into the reactor as a
disturbance. You have potential control over several reactor parameters:
Liquid flows (in and out), Reactor volume, Reactor stirring, … etc.
There are any of several control schemes that can be implemented from simple
PID to MIMO. You are to choose a scheme, collect appropriate data on
dynamics, Implement the scheme and evaluate the resultant controlled dynamics. 9. Polymer Injection Molding InjMold TA: Vikram Daga The obvious purpose of
polymer injection molding is to produce a part (plastic dogbone or spiral)
with certain properties. These properties are subject to testing by an
Instron mechanical testing instrument
(an assigned TA in PSE will run these)
or to other tests you can devise. Normally, the goal is to produce the
strongest part but it could also be to produce a part that breaks within a
given region of force. There are several variables that can be manipulated in
this process that change the strength, uniformity and/or mechanical
performance of the final part. These are ideally suited to experimental
design to optimize this process. We will have several polymers to choose from
for extrusion. You will study one of these in contrast to the other polymers
to be studied by other groups. 10. Polymer Extrusion Extrusion TA: Vikram
Daga A new extruder has been
added to the laboratory that will be more automated than in the past. You can
control many parameters such different temperatures along the barrel of the
extruder. The purpose of polymer extrusion is to produce a continuous strand
of polymer of uniform dimension from pellets. Several dies of varying
dimension are available. The conditions throughout the extruder control the
nature of the product strand. This experiment should first employ
experimental design to optimize the production process and its influence on
dimension and uniformity for different die sizes. You will have several
choices of polymer and will need to characterize the product (dimension and
uniformity). A protocol should be developed for this. Die-swell can be a
complicating factor for certain polymers under specific conditions. We may be
able to develop access to DTA, differential thermal analysis, to characterize differences in the polymer
crystallinity which will depend on process conditions. By employing polymers of different colors,
you may be able to quantify the uniformity of the mixing in the extrusion
process. Do Not start the extruder
until the barrel has been heat up… you would then brake the pin and
loose a period for experiments.
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