Dynamic Optimization and Optimal Control of Hydrogen Blending Operations in Natural Gas Networks
We present a dynamic model for the optimal control problem (OCP) of hydrogen blending into natural gas pipeline networks subject to inequality constraints. The dynamic model is derived using the first principles partial differential equations (PDEs) for the transport of heterogeneous gas mixtures th...
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Main Authors | , , |
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Format | Journal Article |
Language | English |
Published |
05.04.2023
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Subjects | |
Online Access | Get full text |
DOI | 10.48550/arxiv.2304.02716 |
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Summary: | We present a dynamic model for the optimal control problem (OCP) of hydrogen
blending into natural gas pipeline networks subject to inequality constraints.
The dynamic model is derived using the first principles partial differential
equations (PDEs) for the transport of heterogeneous gas mixtures through long
distance pipes. Hydrogen concentration is tracked together with the pressure
and mass flow dynamics within the pipelines, as well as mixing and
compatibility conditions at nodes, actuation by compressors, and injection of
hydrogen or natural gas into the system or withdrawal of the mixture from the
network. We implement a lumped parameter approximation to reduce the full PDE
model to a differential algebraic equation (DAE) system that can be easily
discretized and solved using nonlinear optimization or programming (NLP)
solvers. We examine a temporal discretization that is advantageous for
time-periodic boundary conditions, parameters, and inequality constraint bound
values. The method is applied to solve case studies for a single pipe and a
multi-pipe network with time-varying parameters in order to explore how mixing
of heterogeneous gases affects pipeline transient optimization. |
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Bibliography: | LA-UR-23-23439 |
DOI: | 10.48550/arxiv.2304.02716 |