Abstract

Natural gas processing requires the removal of acidic gases and dehydration using absorption, mainly conducted in tri-ethylene glycol (TEG). The dehydration process is accompanied by the emission of volatile organic compounds, including BTEX. In our previous work, multi-objective optimization was undertaken to determine the optimal operating conditions in terms of the process parameters that can mitigate BTEX emission using data-driven metamodeling and metaheuristic optimization. Data obtained from a process simulation conducted using the ProMax® process simulator were used to develop a metamodel with machine learning techniques to reduce the computational time of the iterations in a robust process simulation. The metamodels were created using limited samples and some underlying phenomena must therefore be excluded. This introduces the so-called metamodeling uncertainty. Thus, the performance of the resulting optimized process variables may be compromised by the lack of adequately accounting for the uncertainty introduced by the metamodel. In the present work, the bias of the metamodel uncertainty was addressed for parameter optimization. An algorithmic framework was developed for parameter optimization, given these uncertainties. In this framework, metamodel uncertainties are quantified using real model data to generate distribution functions. We then use the novel Better Optimization of Nonlinear Uncertain Systems (BONUS) algorithm to solve the problem. BTEX mitigation is used as the objective of the optimization. Our algorithm allows the determination of the optimal process condition for BTEX emission mitigation from the TEG dehydration process under metamodel uncertainty. The BONUS algorithm determines optimal process conditions compared to those from the metaheuristic method, resulting in BTEX emission mitigation up to 405.25 ton/yr.

Highlights

  • Natural gas (NG) obtained from oil and gas wells needs to be sweetened, followed by dehydration for preprocessing to meet sales gas requirements

  • Process simulation was conducted in ProMax®; metamodel generation, error estimation, and uncertainty quantification were performed in MATLAB®; and Better Optimization of Nonlinear Uncertain Systems (BONUS) was conducted in an inhouse optimization module in FORTRAN, installed in a Windows® environment

  • A hybrid algorithm was applied in this work that incorporates support vector regression with the BONUS algorithm for the modeling and optimization of the tri-ethylene glycol (TEG) dehydration process

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Summary

Introduction

Natural gas (NG) obtained from oil and gas wells needs to be sweetened, followed by dehydration for preprocessing to meet sales gas requirements. The wet gas from the NG sweetening process contains, in addition to water, different volatile organic compounds (VOCs), such as toluene, benzene, ethylbenzene, and isomers of xylene, known as BTEX, and is transported to the absorption column where it comes into contact with lean TEG. Rich TEG with water and BTEX flows through a flash tank from the absorption column to the regeneration column. The total BTEX and other VOC emissions from the dehydration process originate from the flash tank and regeneration unit. Metamodels were developed from the simulated process data and metaheuristic optimization to optimize different process variables for BTEX emission reduction and maintain the dry gas specification [1]. An algorithmic framework was developed to address the problem of process variable optimization under metamodel uncertainties. The objective of the optimization process is to mitigate BTEX emission with dry gas water content as a constraint. The effectiveness of our algorithm is shown by the increased value of the stochastic solution (VSS) at lower dry gas water content

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