Process Debottlenecking and Retrofit of Palm Oil Milling Process via Inoperability Input-Output Modelling

In recent years, there has been an increase in crude palm oil (CPO) demand, resulting in palm oil mills (POMs) seizing the opportunity to increase CPO production to make more profits. A series of equipment are designed to operate in their optimum capacities in the current existing POMs. Some equipment may be limited by their maximum design capacities when there is a need to increase CPO production, resulting in process bottlenecks. In this research, a framework is developed to provide stepwise procedures on identifying bottlenecks and retrofitting a POM process to cater for the increase in production capacity. This framework adapts an algebraic approach known as Inoperability Input-Output Modelling (IIM). To illustrate the application of the framework, an industrial POM case study was solved using LINGO software in this work, by maximising its production capacity. Benefit-to-Cost Ratio (BCR) analysis was also performed to assess the economic feasibility. As results, the Screw Press was identified as the bottleneck. The retrofitting recommendation was to purchase an additional Screw Press to cater for the new throughput with BCR of 54.57. It was found the POM to be able to achieve the maximum targeted production capacity of 8,139.65 kg/hr of CPO without any bottlenecks.

[1]  Lorenz T. Biegler,et al.  A mixed integer flowsheet optimization strategy for process retrofits—the debottlenecking problem , 1989 .

[2]  Dominic C.Y. Foo,et al.  Process simulation and debottlenecking for an industrial cocoa manufacturing process , 2011 .

[3]  Adam Baharum,et al.  A Qualitative Approach of Identifying Major Cost Influencing Factors in Palm Oil Mills and the Relations towards Production Cost of Crude Palm Oil , 2011 .

[4]  Damage Pattern and Nesting Characteristic of Coptotermes curvignathus (Isoptera: Rhinotermitidae) in Oil Palm on Peat , 2011 .

[5]  J. J. Klemeš,et al.  An algebraic approach to identifying bottlenecks in linear process models of multifunctional energy systems , 2012, Theoretical Foundations of Chemical Engineering.

[6]  Raymond R. Tan,et al.  Heuristic framework for the debottlenecking of a palm oil-based integrated biorefinery , 2014 .

[7]  Nassim Tahouni,et al.  Debottlenecking of condensate stabilization unit in a gas refinery , 2014 .

[8]  Robin Smith,et al.  Retrofit of heat-integrated crude oil distillation columns , 2015 .

[9]  Masahiko Hirao,et al.  Multiobjective Retrofitting Methodology for Manufacturing Processes of Active Pharmaceutical Ingredients Considering Environment, Health and Safety Risks , 2016 .

[10]  Ana Paula F. D. Barbosa-Póvoa,et al.  Sustainable batch process retrofit design under uncertainty - An integrated methodology , 2017, Comput. Chem. Eng..

[11]  Denny K. S. Ng,et al.  Design Operability and Retrofit Analysis (DORA) framework for energy systems , 2017 .