4.5 Article

Simulation, optimization, and economic analysis of process to obtain esters from fatty acids

Journal

BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR
Volume 15, Issue 3, Pages 749-769

Publisher

WILEY
DOI: 10.1002/bbb.2186

Keywords

simulation; kinetic modeling; esterification and transesterification; hydrous ethanol; process optimization; economic analysis

Funding

  1. Conselho Nacional de Desenvolvimento Cientifico e Tecnologico (CNPq) [309181/2019-4]
  2. Coordenacao de Aperfeicoamento de Pessoal de Nivel Superior - Brazil (CAPES) [001]

Ask authors/readers for more resources

This study experimentally tested different acid-catalyzed esterification reaction conditions with varying water concentrations, proposing a new rate expression for the reaction kinetics in biodiesel production from waste oils. Process modifications such as energy-saving heat exchangers and ethanol-recycling distillation column were found to significantly reduce utility costs and raw material costs by 40% respectively, resulting in a payback period of less than 3 years in any evaluated scenario.
Waste oils are a very promising raw material in the biodiesel industry, which is why great efforts have focused on the removal of the free fatty acids (FFAs) present in this source, mainly through the esterification reaction. Many studies have evaluated the influence of different variables on the reaction conversion, such as temperature, catalyst concentration, and alcohol/oil ratio. However, it is still necessary to verify how the esterification is affected by higher water concentration. In this study, different acid-catalyzed esterification reaction conditions with distinct water concentrations were tested experimentally, and a new rate expression was proposed. This newly obtained reaction kinetics was then used to undertake a complete analysis of the biodiesel production process from waste oil, evaluating the influence of higher water concentrations in the esterification, and including different optimizations and an economic evaluation. Concerning some of the process modifications, it was verified that the inclusion of three energy-saving heat exchangers reduced utility costs by 40%. In contrast, the inclusion of an ethanol-recycling distillation column reduced raw material costs by 40%. Different settings were also tested, varying the feed composition and the esterification reaction time and conditions, resulting in a payback period of less than 3 years in any evaluated scenario. (c) 2021 Society of Chemical Industry and John Wiley & Sons, Ltd

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.5
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available