An energy hub, which receives, converts, stores and delivers different energy carriers by means of variety of energy converters and/or storage elements, is one of the most important concepts in multi-carrier energy systems. For cost-effective and reliable supply of energy to loads in multi-carrier energy systems, the problem of selecting different components forming the hub (referred to as hub design) and their operation is of great importance. In this paper, a comprehensive linearized model for optimal design and operation of energy hubs considering reliability constraints is proposed. Adequacy indices and maximum allowable loss of load probability (LOLP) in case of single contingency are checked and different reliability constraints are introduced in the optimization process to satisfy the required level of reliability for different load types. Finally, the proposed method is applied on a test case considering electrical and thermal loads. Obtained results show the ability of the proposed method in meeting energy demand while respecting reliability constraints.Index terms--Adequacy, energy hub, energy storage, reliability NOMENCLATURE The main notation used throughout this paper is stated below. Other symbols are defined as needed. Indices: UB ELNS Upper bound of ELNS. UB EENS Upper bound of EENS. UB LOLE Upper bound of LOLE.
Sequential model-based design of experiments (MBDoE) uses information from previous experiments to select new experimental conditions. Computation of MBDoE objective functions can be impossible due to a noninvertible Fisher information matrix (FIM). Previously, we evaluated a leave-out (LO) approach that designed experiments by removing problematic model parameters from the design process. Unfortunately, the LO approach can be computationally expensive due to its iterative nature. In this study, we propose a simplified Bayesian approach that makes the FIM invertible by accounting for prior parameter information. We compare the proposed simplified Bayesian approach to the LO approach for sequential A-optimal design. Results from a pharmaceutical case study show that the proposed approach is superior, on average, for design of experiments. We suggest that simplified Bayesian MBDoE should be combined with a subset-selection-based approach for parameter estimation. This combined methodology gave the best results on average for the case study.
The sequential model-based optimal
design of experiments (e.g., A-, D-, and E-optimal design) is a well-known
technique for selecting experimental conditions that lead to informative
data for obtaining reliable parameter estimates and model predictions.
An important computational step for selecting new model-based experiments
is to compute the inverse of the Fisher information matrix (FIM) which may not be invertible. In this study, three different
methodologies for selecting new experiments are compared for situations
where the FIM is noninvertible. The first approach finds
and leaves out problematic parameters that make FIM noninvertible
and then designs experiments using a reduced FIM (LO
approach). The second approach uses a Moore-Penrose pseudoinverse
of the FIM in A-optimal design calculations (PI approach).
The third methodology is an ad hoc approach which
does not require optimization. In this MS approach, the modeler selects
settings at corners of the specified design space. Comparisons are
made using two linear regression models and a nonlinear dynamic model
for production of a pharmaceutical agent. Monte Carlo simulation results
show that experimental settings obtained by LO and PI approaches give
better parameter estimates on average than the MS approach, with the
LO approach giving the best estimates in 20 of 24 linear situations
studied. The LO approach also gives the best parameter estimates on
average for the nonlinear pharmaceutical model.
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Highlights Sequential model-based design of experiments results in informative experimental data for estimating parameters and making predictions using fundamental models. Inversion of Fisher Information Matrix (FIM) is required for model-based design of experiments. The FIM may be noninvertible for complex chemical and pharmacological process models. Parameter subset selection leaves out problematic parameters, resulting in a reduced FIM that is effective for experimental design.
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