Superstructure-based Design and Optimization of Batch Biodiesel Production Using Heterogeneous Catalysts

International Research and Innovation Summit 2017

Nuh, M.Z.^1 ; Nasir, N.F.^1

Faculty of Mechanical and Manufacturing Engineering, University Tun Hussein Onn Malaysia (UTHM), Johor, Batu Pahat

86400, Malaysia^1

关键词: Complex engineering system;    Design and optimization;    Heterogeneous catalyst;    Long chain fatty acid;    Mixed-integer nonlinear programming;    Process system engineering;    Superstructure optimization;    Tools and techniques;   

Others  :  https://iopscience.iop.org/article/10.1088/1757-899X/226/1/012001/pdf
DOI  :  10.1088/1757-899X/226/1/012001

来源: IOP

【 摘 要 】

Biodiesel as a fuel comprised of mono alkyl esters of long chain fatty acids derived from renewable lipid feedstock, such as vegetable oil and animal fat. Biodiesel production is complex process which need systematic design and optimization. However, no case study using the process system engineering (PSE) elements which are superstructure optimization of batch process, it involves complex problems and uses mixed-integer nonlinear programming (MINLP). The PSE offers a solution to complex engineering system by enabling the use of viable tools and techniques to better manage and comprehend the complexity of the system. This study is aimed to apply the PSE tools for the simulation of biodiesel process and optimization and to develop mathematical models for component of the plant for case A, B, C by using published kinetic data. Secondly, to determine economic analysis for biodiesel production, focusing on heterogeneous catalyst. Finally, the objective of this study is to develop the superstructure for biodiesel production by using heterogeneous catalyst. The mathematical models are developed by the superstructure and solving the resulting mixed integer non-linear model and estimation economic analysis by using MATLAB software. The results of the optimization process with the objective function of minimizing the annual production cost by batch process from case C is $23.2587 million USD. Overall, the implementation a study of process system engineering (PSE) has optimized the process of modelling, design and cost estimation. By optimizing the process, it results in solving the complex production and processing of biodiesel by batch.