Abstract
Biodiesel is one of the most prominent biofuels in the market, recent trends indicate a worldwide production growth to replace crude-based diesel as transportation fuel. In this work, two reactive distillation processes with their corresponding downstream separation units are simulated: the first involves alkali whereas the second includes heterogeneous catalyst. The processes yield a high purity biodiesel product. Aspen Plus v8.4 was used as the process simulation tool in the present work. Comparison between the two production processes were made in terms of the annual production costs and economic indicators such as Return-On-Investment (ROI) and payback period. The simulation results show that the heterogeneous-catalyzed process is more economically advantageous than the alkali-catalyzed process for biodiesel production due to a much higher ROI, lower payback period, and lower annual cost per unit of biodiesel produced.
| Original language | British English |
|---|---|
| Pages (from-to) | 17-22 |
| Number of pages | 6 |
| Journal | Energy Procedia |
| Volume | 75 |
| DOIs | |
| State | Published - 2015 |
| Event | 7th International Conference on Applied Energy, ICAE 2015 - Abu Dhabi, United Arab Emirates Duration: 28 Mar 2015 → 31 Mar 2015 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- Biodiesel
- Process Simulation
- Reactive Distillation
- Transesterification
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