Page 52 - ASME DSCC 2015 Program
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Technical Program




                                                                     natural Gas Hydrogen Reformer Controller Design With Disturbance
              ConTRIBuTED SESSIon
              1-10-1  TM4  natural Gas and Heat Exchangers           Rejection
              Geroge Bellows f                        1:30pm–3:30pm  Contributed regular paper. DSCC2015-9970
                                                                     Verica Gajic, Patrick Rose, Villanova Univerisity, Villanova, PA, United
              Session Chair: Bryan Keating, University of Illinois at Urbana Champaign  States
              Session Co-Chair: xingyong Song, Halliburton Energy Service Co
                                                                     In this paper we present a controller design for a linearized model of a fuel
                                                                     cell hydrogen gas reformer, which produces hydrogen from natural gas. We
              Modeling of Ionic Polymer-Metal Composite-Enabled Hydrogen Gas
                                                                     design two feedback control loops, one of them with an integrator and an-
              Production
                                                                     other one with proportional state feedback. In the third step, a feed-forward
              Contributed regular paper. DSCC2015-9922
                                                                     controller is designed whose role is to off-set for the impact of the distur-
              Tushar nagpure, Zheng Chen, Wichita State University, Wichita, KS, United   bance represented by the fuel cell current. Both the feedback controller and
              States
                                                                     the feed-forward controller are obtained through a rigorous dynamic opti-
              Hydrogen extraction using water electrolysis, and microbial biomass conver-  mization process of a quadratic performance criterion along trajectories of
              sion are clean and minimum-emission option for renewable energy storage   a linear dynamic system. According to the presented simulation results, the
              applications. Ionic polymer-metal composite (IPMC) is a category of elec-  proposed controller copes well with the disturbance and reduces its impact
              tro-active polymers that exhibits the property of ion migration under the ap-  within a few seconds from the time when the disturbance occurs, despite
              plication of external voltage. This property of IPMC is useful in electrolysis of   large jumps in the fuel cell current (disturbance).
              water (H2O) and produce hydrogen (H2) and oxygen (O2) gases. This paper
                                                                     Model Reduction and optimization of natural Gas Pipeline Dynamics
              discusses the electrochemical fundamentals of electrolysis, which provides
                                                                     Contributed regular paper. DSCC2015-9683
              a linear relationship between the flow rate of hydrogen from electrolysis and
                                                                     Anatoly Zlotnik, Scott Backhaus, Michael Chertkov, Los Alamos National
              the source current. An IPMC electrolyzer circuit model is developed to cap-
                                                                     Laboratory, Los Alamos, NM, United States, Sergey Dyachenko, The
              ture the electrical characteristic of IPMC. The model incorporates nonlinear
                                                                     University of Arizona, Tucson, AZ, United States
              capacitance, pseudo-capacitance, and a nonlinear resistance defined with a
              polynomial function. A state-space equation is then obtained to simulate the   We derive a reduced control system model for the dynamics of compress-
              proposed circuit model for electrolysis. Experimental result shows that the   ible gas flow through a pipeline subject to distributed time-varying injections,
              flow-rate of hydrogen production is proportional to the system current and   withdrawals, and control actions of compressors.  The gas dynamics PDE
              the proposed model validates the step-response of the system. The model   equations are simplified using lumped elements to a nonlinear ODE system
              prediction error is less than 4.5647%.                 with matrix coefficients.  We verify that low-order integration of this ODE
                                                                     system with adaptive time-stepping is computationally consistent with solu-
              Wiener Modeling of a Closed loop Vapor Compression System for
                                                                     tion of the PDE system using a split-step characteristic scheme on a regular
              Extremum Seeking Control Design
                                                                     space-time grid for a realistic pipeline model.  Furthermore, the reduced
              Contributed regular paper. DSCC2015-9941
                                                                     model is tractable for use as the dynamic constraints of the optimal control
              Bryan Keating, Justin P. Koeln, Andrew G. Alleyne, University of Illinois at   problem of minimizing compression costs given transient withdrawals and
              Urbana-Champaign, Urbana, IL, United States            gas pressure constraints.  We discretize this problem as a finite nonlinear
              This paper demonstrates that the dynamic relationship between the power   program using a pseudospectral collocation scheme, which we solve to
              consumption of a vapor compression system under closed loop control and   obtain a polynomial approximation of the optimal transient compression
              its evaporator and condenser fan inputs is well described about a nominal   controls.  The method is applied to an example involving the Williams-
              operating point by a Wiener model, which is useful for extremum seeking   Transco pipeline.
              controller design. Information about the input dynamics from the Wiener
                                                                     Dynamic Modeling of Heat Exchangers With Humidity and
              model is used to evaluate the tradeoff between steady-state error and
                                                                     Condensation
              convergence time for single and dual input extremum seeking controllers in
                                                                     Contributed regular paper. DSCC2015-9646
              simulation.
                                                                     Herschel Pangborn, Andrew G. Alleyne, University of Illinois at Urbana-
                                                                     Champaign, Urbana, IL, United States
                                                                     The effects of air humidity on the performance of refrigerant-to-air heat ex-
                                                                     changers in vapor compression systems (VCSs) are non-negligible in model-
                                                                     ing and control design for some applications. Such applications include both
                                                                     those in which the ambient humidity is expected to vary greatly over time
                                                                     and those in which control of the air outlet humidity is desired. This paper
                                                                     presents a control-oriented dynamic model for cross-flow refrigerant-to-air
                                                                     heat exchangers that uses knowledge of the air inlet humidity to improve the
                                                                     accuracy of refrigerant-side and air-side outputs, as well as to calculate the
                                                                     air outlet humidity and rate of condensate formation. Simulation results are
                                                                     validated with experimental data collected from a 1kW VCS test stand.
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