Performance analysis of dividing wall column model for fractionation of oleochemical fatty acid


Citation

Mohamad Rizza Othman, . and Rangaiah Gade Pandu, . Performance analysis of dividing wall column model for fractionation of oleochemical fatty acid. pp. 326-340. ISSN 1511-2780

Abstract

Fractionation process of oleochemical products in Malaysia normally uses conventional distillation columns (CDC). Due to the considerable amount of energy used in the separation process there is a need to have an intensified process. Dividing wall column (DWC) is an attractive option which offers big advantages with reduced cost and energy consumption. However research on its feasibility for oleochemical fractionation is scarce. In this article we conducted a model-based performance analysis of DWC for oleochemical fatty acid fractionation. The model was designed and simulated using a customised four column configurations in Aspen Plus. A step-by-step design procedure was introduced to aid the model development. Economic and environmental assessment was performed and compared with conventional distillation columns. Hydraulic analysis of several packing type was also performed to gain insights on the column hydrodynamic behaviour. Our result shows that the major economic advantage is in the operating cost with savings of up to 16.9 and 10.2 on cooling and heating utilities respectively while reduces 10.2 of CO‚‚ emissions. Overall our study shows the feasibility of fractionating fatty acids in oleochemical industry using DWC. Such assessment is important to assess its feasibility especially during the early stage of technology development prior to industrial implementation.


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Abstract

Fractionation process of oleochemical products in Malaysia normally uses conventional distillation columns (CDC). Due to the considerable amount of energy used in the separation process there is a need to have an intensified process. Dividing wall column (DWC) is an attractive option which offers big advantages with reduced cost and energy consumption. However research on its feasibility for oleochemical fractionation is scarce. In this article we conducted a model-based performance analysis of DWC for oleochemical fatty acid fractionation. The model was designed and simulated using a customised four column configurations in Aspen Plus. A step-by-step design procedure was introduced to aid the model development. Economic and environmental assessment was performed and compared with conventional distillation columns. Hydraulic analysis of several packing type was also performed to gain insights on the column hydrodynamic behaviour. Our result shows that the major economic advantage is in the operating cost with savings of up to 16.9 and 10.2 on cooling and heating utilities respectively while reduces 10.2 of CO‚‚ emissions. Overall our study shows the feasibility of fractionating fatty acids in oleochemical industry using DWC. Such assessment is important to assess its feasibility especially during the early stage of technology development prior to industrial implementation.

Additional Metadata

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Item Type: Article
AGROVOC Term: Fatty acids
AGROVOC Term: Energy use
AGROVOC Term: Fractionation
AGROVOC Term: Separation
AGROVOC Term: Models
AGROVOC Term: Physical properties
AGROVOC Term: Operating costs
AGROVOC Term: Simulation
AGROVOC Term: Purification
AGROVOC Term: Environmental assessment
Depositing User: Mr. AFANDI ABDUL MALEK
Last Modified: 24 Apr 2025 00:54
URI: http://webagris.upm.edu.my/id/eprint/9165

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