The research done by the group centers around the development and application of concepts in optimization theory, operations research, and numerical methods for process design, analysis, and control.
Topic: Pressure swing adsorption optimization strategies for CO2 capture
Pressure swing adsorption (PSA) has received recent attention as a potential process for economically removing CO2 from flue and/or shifted syngas for carbon capture and storage. We apply state-of-the-art methods for PSA optimization using a superstructure-based approach; this allows simultaneous selection of PSA cycle steps and optimization of operating parameters (feed flow rate, recycle fractions, bed pressures, etc.). The partial differential equation bed models are discretized with finite volumes in space and two flux limiters are compared. Sparse linear solvers are implemented to accelerate the integration of bed models and direct sensitivity equations, which are interfaced to MATLAB. The PSA optimization approach is demonstrated on CO2/H2 separation case studies for an integrated gasification combine cycle power plant, and solved by sequential quadratic programming solvers.
Topic: Modeling and optimal grade transitions for polypropylene processes in fluidized bed reactors
Gas phase polymerizations using fluidized bed reactors are widely implemented in industry. We present a set of differential and algebraic equations to simulate this process for producing polypropylene. Kinetic models based on multisite catalysts (Ziegler-Natta) are used for propylene and ethylene copolymerization. This work will lead to the grade transition optimization, shortening the transition time by manipulating operation conditions.
Topic: Advanced Optimal Control Strategies for Bubbling Fluidized Beds
Bubbling Fluidized Bed (BFB) models have been previously created for CO2 capture. Such models contain Partial Differential Equations to model the mass and energy balances for different regions inside the bed. Additionally there are Algebraic Equations to model the hydrodynamics, equations of state, etc. This leads to a system of Partial Differential Equations (PDAE) that can be handled through an implicit high order discretization scheme like collocation.
The availability of such models and new algebraic modeling languages like Pyomo, make possible the implementation of Non-Linear Model Predictive Control (NMPC) strategies for the BFB.
The goals of the project are to generate steady and dynamic state models for the BFB with generic discretization schemes and to implement fast NMPC and state estimation strategies.
Topic: Multistage Nonlinear Model Predictive Control under Uncertainty
Model Predictive Control (MPC) has been widely used in process control industry mainly because it can deal with constraints and multiple-input-multiple-output. However, the system performance deteriorates under the influence of uncertainty. The current robust MPC techniques are often shy of applications due to either model conservativeness or formidable computational effort. In order to improve this situation, we present a multistage nonlinear model predictive control (NMPC) to serve as a non-conservative robust NMPC scheme. Multistage NMPC models the uncertainty evolution with a scenario tree structure that exploits the degree of freedom by allowing future control inputs to adjust accordingly to future available information.
Currently, our case study is based on a nonlinear CSTR example with a setpoint tracking objective with one uncertain parameter. The performance of multistage NMPC has been compared to standard NMPC and no-recourse robust NMPC, and the result shows that multistage NMPC is a promising framework to account for plant uncertainty. The effect of different robust horizons has also been discussed.
Topic: Optimization Superstructure Development for Rigid Polyols
Rigid polyols are defined as polyether polyols formed by catalyzed alkoxylation of initiators. These polyols react with isocyanates to manufacture closed cell foams which are used in the production of refrigerators and freezers, building and construction insulation, etc. Demand has doubled in the last 10 years and is expected to double again in the next 10 years. Rigid polyols are currently produced in semi-batch reactors. As product demand grows, the business is faced with investing in more or larger semi-batch reactors which will reduce the capital cost per production, but this is still too high for re-investment relative to other products. Lower capital cost solutions, such as transfer the production from existing semi-batch units to continues process, are needed to help sustain growth. Continuous reactors can decrease the capital cost if a scheme can be devised to produce similar products. In order to determine if this is possible, simulation and optimization can be used with reaction kinetics to determine the required number, type and size of reactors to achieve product specifications with minimal cost.
Topic: Non-Smooth Process Optimization using Complementarity Constraints.
Process Intensification is currently the most important aspect for chemical industry to decrease energy consumption and harmful gas emissions. As more complex and rigorous process models are developed to achieve this goal, there is a need to develop solution strategies for optimizing these process models. Most process models suffer from discontinuities and non-differentiability making it difficult to solve them using common optimization solvers. We model these non-smooth equations using complementarity constraints. Mathematical Programming with Complementarity Constraints(MPCC) and Nonlinear programming(NLP) are powerful tools to solve optimization problems without introducing complex integer variables. We use various methods from MPCC literature and implement in solving large scale chemical process models. Currently, we are using finite element heat exchanger model to optimize refrigeration cycles. The phase change inside the heat exchangers is modeled by complementarity constraints. The MPCC problem is reformulated and solved successively as a NLP. In future, we will integrate this MPCC solution framework into more complicated models.
Topic: Optimization for continuous multiple product processes.
Continuous multiple product processes are commonly observed in the chemical industry such as halogenation of aromatics. The process has the following two aspects. One is the process is usually large because it consists of multiphase reactors such as bubble columns, and several separation units such as distillations, absorbers, and crystallizers. This aspect leads to large-scale process modeling which contains Differential Algebraic Equations (DAEs). Another is the balance of product demand could vary from time to time because the products are used as raw materials in widely different fields. From this aspect, the process optimization is to be considered under uncertainty. From these characteristics, the goals of the project are to model the large-scale process flow and to optimize the process under uncertainty of its product demand. Currently, a bubble column reactor in which take place chlorination of an aromatic is modeled in Pyomo.