TY - GEN
T1 - Optimization of petlyuk distillation column design of multi-component mixtures separation process using stochastic optimization algorithm
AU - Haksoro, Toto
AU - Asianingsih, Yelinda
AU - Mujiyanti, Safira Firdaus
AU - Aisjah, Aulia Siti
AU - Biyanto, Totok Ruki
N1 - Publisher Copyright:
© 2019 American Institute of Physics Inc. All rights reserved.
PY - 2019/3/29
Y1 - 2019/3/29
N2 - Distillation process is a process which involves a separation of two or more components. The most crucial issue in distillation process is the excessive usage of energy. Therefore, Petlyuk distillation column design and the right optimization method is highly needed to overcome the issue. The purpose of this research is aimed to design a Petlyuk distillation column based on a few methods such as a shortcut method, a modified shortcut method and Vapor-Liquid Equilibrium (VLE). The result of VLE is being optimized using a few of stochastic optimization algorithms such as Genetic Algorithm (GA), Imperialist Competitive Algorithm (ICA), Particle Swarm Optimization (PSO) and Duelist Algorithm (DA). From the result obtained, a Petlyuk distillation column designed using shortcut method, modified shortcut method and VLE are able to reduce the Total Annual Cost (TAC) by 30.16%, 36.03%, and 43.90% respectively. Besides, the design of distillation column could affect the total energy required, capital cost, operational cost, and the quality of the product. VLE method which optimized by PSO is observed could reduce the TAC by 45.76%. Moreover, the composition is observed to be approximately equal to the actual data which are 0.05775, 0.94925 and 0.38469 for ethane, propane, and n-butane.
AB - Distillation process is a process which involves a separation of two or more components. The most crucial issue in distillation process is the excessive usage of energy. Therefore, Petlyuk distillation column design and the right optimization method is highly needed to overcome the issue. The purpose of this research is aimed to design a Petlyuk distillation column based on a few methods such as a shortcut method, a modified shortcut method and Vapor-Liquid Equilibrium (VLE). The result of VLE is being optimized using a few of stochastic optimization algorithms such as Genetic Algorithm (GA), Imperialist Competitive Algorithm (ICA), Particle Swarm Optimization (PSO) and Duelist Algorithm (DA). From the result obtained, a Petlyuk distillation column designed using shortcut method, modified shortcut method and VLE are able to reduce the Total Annual Cost (TAC) by 30.16%, 36.03%, and 43.90% respectively. Besides, the design of distillation column could affect the total energy required, capital cost, operational cost, and the quality of the product. VLE method which optimized by PSO is observed could reduce the TAC by 45.76%. Moreover, the composition is observed to be approximately equal to the actual data which are 0.05775, 0.94925 and 0.38469 for ethane, propane, and n-butane.
UR - http://www.scopus.com/inward/record.url?scp=85064391679&partnerID=8YFLogxK
U2 - 10.1063/1.5095253
DO - 10.1063/1.5095253
M3 - Conference contribution
AN - SCOPUS:85064391679
T3 - AIP Conference Proceedings
BT - Advanced Industrial Technology in Engineering Physics
A2 - Hatta, Agus Muhamad
A2 - Indriawati, Katherin
A2 - Nugroho, Gunawan
A2 - Biyanto, Totok Ruki
A2 - Arifianto, Dhany
A2 - Risanti, Doty Dewi
A2 - Irawan, Sonny
PB - American Institute of Physics Inc.
T2 - 2nd Engineering Physics International Conference 2018, EPIC 2018
Y2 - 31 October 2018 through 2 November 2018
ER -