CATEGORY: PROCESS CONTROL
THESIS
Advanced
And Novel Modeling Techniques For Simulation, Optimization And Monitoring
Chemical Engineering Tasks With Refinery And Petrochemical Unit Applications
Gregory Robertson
A Dissertation Submitted to the Graduate Faculty of the Louisiana State
University and Agricultural and Mechanical College in partial fulfillment of
the requirements for the degree of Doctor of Philosophy in The Department of
Chemical Engineering (2014)
Abstract
Engineers predict, optimize, and monitor processes to improve safety and profitability.
Models automate these tasks and determine precise solutions. This research
studies and applies advanced and novel modeling techniques to automate and aid
engineering decision-making.
Advancements in computational ability have improved modeling software’s ability
to mimic industrial problems. Simulations are increasingly used to explore new
operating regimes and design new processes. In this work, we present a
methodology for creating structured mathematical models, useful tips to
simplify models, and a novel repair method to improve convergence by populating
quality initial conditions for the simulation’s solver. A crude oil refinery
application is presented including simulation, simplification tips, and the
repair strategy implementation. A crude oil scheduling problem is also
presented which can be integrated with production unit models.
Recently, stochastic global optimization (SGO) has shown to have success of
finding global optima to complex nonlinear processes. When performing SGO on
simulations, model convergence can become an issue. The computational load can
be decreased by 1) simplifying the model and 2) finding a synergy between the
model solver repair strategy and optimization routine by using the initial
conditions formulated as points to perturb the neighborhood being searched.
Here, a simplifying technique to merging the crude oil scheduling problem and
the vertically integrated online refinery production optimization is
demonstrated. To optimize the refinery production a stochastic global
optimization technique is employed.
Process monitoring has been vastly enhanced through a data-driven modeling
technique Principle Component Analysis. As opposed to first-principle models,
which make assumptions about the structure of the model describing the process,
data-driven techniques make no assumptions about the underlying relationships.
Data-driven techniques search for a projection that displays data into a space
easier to analyze. Feature extraction techniques, commonly dimensionality
reduction techniques, have been explored fervidly to better capture nonlinear
relationships. These techniques can extend data-driven modeling’s
process-monitoring use to nonlinear processes. Here, we employ a novel
nonlinear process-monitoring scheme, which utilizes Self-Organizing Maps. The
novel techniques and implementation methodology are applied and implemented to
a publically studied Tennessee Eastman Process and an industrial polymerization
unit.
Thesis Focus
In
an effort to automate and improve decision-making, chemical engineers create
tools to aid their goals of predictability, profitability, and safety. Process
control engineers specifically perform predicting, optimizing, and process
monitoring tasks. Complex mathematical models are solved through a computationally
expensive iterative procedure. With advancements of computational ability,
modeling software’s ability to mimic industrial problems has improved
significantly. This has allowed engineers to push the boundaries of the size,
complexity and detail of the engineering problems they model to make process
decisions with a vastly improved level of accuracy.
The purpose of this research is to study and apply advanced and
novel mathematical modeling techniques to aid in solving chemical engineering
problems. A large amount of the creativity of this work has been not only in
the designing methodology, but also in overcoming practical implementation
difficulties.
Free Full Text Source: http://etd.lsu.edu/docs/available/etd-01222014-142700/
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