Stochastic-Based Optimization Strategy of Dimethyl Oxalate Hydrogenation for Ethylene Glycol Production

The multi-objective optimization (MOO) of ethylene glycol (EG) production in a hydrogenation tubular reactor focuses on two main objectives: increasing yield and reducing energy cost. A model-based optimization approach using the ASPEN Plus simulator was employed to simulate the reactions. In additi...

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Veröffentlicht in:Process integration and optimization for sustainability 2024-09, Vol.8 (4), p.1149-1162
Hauptverfasser: Rohman, Fakhrony Sholahudin, Alwi, Sharifah Rafidah Wan, Kelani, Rasheed Olakunle, Muhammad, Dinie, Azmi, Ashraf, Murat, Muhamad Nazri
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container_title Process integration and optimization for sustainability
container_volume 8
creator Rohman, Fakhrony Sholahudin
Alwi, Sharifah Rafidah Wan
Kelani, Rasheed Olakunle
Muhammad, Dinie
Azmi, Ashraf
Murat, Muhamad Nazri
description The multi-objective optimization (MOO) of ethylene glycol (EG) production in a hydrogenation tubular reactor focuses on two main objectives: increasing yield and reducing energy cost. A model-based optimization approach using the ASPEN Plus simulator was employed to simulate the reactions. In addition, an inequality constraint was imposed on the reactor temperature to prevent a runaway condition. To solve the optimization problems, three multi-objective stochastic optimization algorithms, which are the multi-objective stochastic paint optimizer (MOSPO), multi-objective slime mold algorithm (MOSMA), and multi-objective dragonfly algorithm (MODA), were utilized along with MATLAB and ASPEN Plus simulator. In addition, performance metrics including hypervolume (H), pure diversity (PD), and spacing (S) were employed to evaluate and decide the most effective MOO approach. The results show that the most effective MOO approach for EG production in a hydrogenation tubular reactor is MODA. Its solution set provides precise, diverse, and well-distributed allocation of ND points along the Pareto Front (PF). Also, the results indicate that the highest productivity, lowest energy cost, and highest yield achieved are RM41.3499 million/year, RM0.1667 million/year, and 95.5249%, respectively. Furthermore, the plots of decision variables demonstrate that the reactor pressure highly impacts the optimal solution.
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A model-based optimization approach using the ASPEN Plus simulator was employed to simulate the reactions. In addition, an inequality constraint was imposed on the reactor temperature to prevent a runaway condition. To solve the optimization problems, three multi-objective stochastic optimization algorithms, which are the multi-objective stochastic paint optimizer (MOSPO), multi-objective slime mold algorithm (MOSMA), and multi-objective dragonfly algorithm (MODA), were utilized along with MATLAB and ASPEN Plus simulator. In addition, performance metrics including hypervolume (H), pure diversity (PD), and spacing (S) were employed to evaluate and decide the most effective MOO approach. The results show that the most effective MOO approach for EG production in a hydrogenation tubular reactor is MODA. Its solution set provides precise, diverse, and well-distributed allocation of ND points along the Pareto Front (PF). Also, the results indicate that the highest productivity, lowest energy cost, and highest yield achieved are RM41.3499 million/year, RM0.1667 million/year, and 95.5249%, respectively. 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subjects Algorithms
Economics and Management
Energy
Energy costs
Energy Policy
Engineering
Ethylene glycol
Exploitation
Fluidized bed reactors
Hydrogenation
Industrial and Production Engineering
Industrial Chemistry/Chemical Engineering
Multiple objective analysis
Optimization
Original Research Paper
Pareto optimization
Performance measurement
Production capacity
Reactors
Slime molds
Stochasticity
Sustainable Development
Variables
Waste Management/Waste Technology
title Stochastic-Based Optimization Strategy of Dimethyl Oxalate Hydrogenation for Ethylene Glycol Production
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