<abstract xmlns="http://www.w3.org/1999/xhtml"><p>To investigate the effect of reactor performance/configuration of biodiesel production on process parameters (mass &amp; energy consumption, required facilities etc.), two diverse production processes (from vegetable oil) were implemented/designed using Aspen HYSYS V7.2. Two series reactors were taken into account where overall conversion was set to be 97.7% and 70% in first and second processes respectively. Comparative analysis showed that an increase in conversion yield caused to consumption reduction of oil, methanol, cold energy and hot energy up to 9.1%, 22%, 67.16% and 60.28% respectively; further, a number of facilities (e.g. boiler, heat exchanger, distillation tower) were reduced. To reduce mass &amp; energy consumption, mass/heat integration method was employed. Applying integration method showed that in the first design, methanol, cold and hot energy were decreased by 49.81%, 17.46% and 36.17% respectively; while in the second design, oil, methanol, cold and hot energy were decreased by 9%, 60.57% 19.62% and 36.58% respectively.</p></abstract>

To investigate the effect of reactor performance/configuration of biodiesel production on process parameters (mass & energy consumption, required facilities etc.), two diverse production processes (from vegetable oil) were implemented/designed using Aspen HYSYS V7.2. Two series reactors were taken into account where overall conversion was set to be 97.7% and 70% in first and second processes respectively. Comparative analysis showed that an increase in conversion yield caused to consumption reduction of oil, methanol, cold energy and hot energy up to 9.1%, 22%, 67.16% and 60.28% respectively; further, a number of facilities (e.g. boiler, heat exchanger, distillation tower) were reduced. To reduce mass & energy consumption, mass/heat integration method was employed. Applying integration method showed that in the first design, methanol, cold and hot energy were decreased by 49.81%, 17.46% and 36.17% respectively; while in the second design, oil, methanol, cold and hot energy were decreased by 9%, 60.57% 19.62% and 36.58% respectively.

Biodiesel production from vegetable oil: Process design, evaluation and optimization

Biotechnology Research Center, Faculty of Chemical Engineering

Amirkabir University of Technology (TehranPolytechnic)

Polish Journal of Chemical Technology

This work is licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 3.0 License.

To investigate the effect of reactor performance/configuration of biodiesel production on process parameters (mass & energy consumption, required facilities...

Biodiesel production from vegetable oil: Process design, evaluation and optimization

Publié en ligne: 10 oct. 2017

Pages: 49 - 55

DOI: https://doi.org/10.1515/pjct-2017-0048

Mots clés
Process Design, Heat & Mass Integration, Biodiesel, Pinch Technology, Heat Exchanger Network

© 2017 Hamid Reza Kianimanesh et al., published by De Gruyter Open

This work is licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 3.0 License.

Biodiesel production from vegetable oil: Process design, evaluation and optimization

Publié en ligne: 10 oct. 2017

Pages: 49 - 55

DOI: https://doi.org/10.1515/pjct-2017-0048

Mots clésProcess Design, Heat & Mass Integration, Biodiesel, Pinch Technology, Heat Exchanger Network

© 2017 Hamid Reza Kianimanesh et al., published by De Gruyter Open

This work is licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 3.0 License.

Mots clés
Process Design, Heat & Mass Integration, Biodiesel, Pinch Technology, Heat Exchanger Network