Design and Integration for Biodiesel Production from Vegetable Oil via Transesterification Reaction (Brief Report)

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Abbaspour Aghdam F.; KIANIMANESH H.R.; ARABIAN D.; KHALILZADEH R.

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Paper Information

Journal: JOURNAL OF AGRICULTURAL MACHINERY Year:2018 | Volume:8 | Issue:1 (15) Page(s): 223-234

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Title

Design and Integration for Biodiesel Production from Vegetable Oil via Transesterification Reaction (Brief Report)

Author(s)

Abbaspour Aghdam F. | KIANIMANESH H.R. | ARABIAN D. | KHALILZADEH R. | Issue Writer Certificate

Keywords

Biodiesel process designQ1

Integration and simulationQ1

Heat exchangers networkQ1

Pinch technologyQ1

Vegetable oilQ1

Abstract

Introduction: Biodiesel is Fatty Acid Methyl Esters (FAME) which is used as a renewable fuel in diesel engines. Extraction of lipid from various flora sources, including Sunflower, Palm, Canola or animal oils, with a Trans-Esterification reaction between alcohol and Triglyceride (TG), leads to production of Biodiesel and Glycerin. The production cost of biodiesel is so important that is now considered as the greatest obstacle during scaleup process. In this research, a model-type of biodiesel production unit (using Vegetable oil source), was designed by Aspen HYSYS V7. 2 software, then a great deal of the attempt was employed to optimize the overall yield against the processing parameters including: mass and energy consumption load, as well as some technical discussion regarding associated apparatuses. Materials and Methods: Process Design: The simulation was carried out using Aspen HYSYS V7. 2 employing Triolein (as TG), Oleic acid (as Free Fatty Acid (FFA)), and Oleat as biodiesel. Avoiding side-stream reactions as well as trans-esterification, the FFA content was taken to a mere 0. 05% (%mass). Feed stream was considered as product of NaOH-catalyzed bireactor system operating at 60˚ C and 1 atm with the overall conversion of 70% using two series reactors. The ratio of TG to Alcohol is 1: 3, however, owing to establish an appropriate reactor performance; this ratio was applied as 1: 6 practically. The design was mainly intended to produce 480 m3d-1 biodiesel with mass concentration of 99. 65%. Methanol was used in this investigation due to low cost, accessibility and handling considerations. NRTL was taken as the Equation of State (EOS) for the process and should be used PRSV equation in the decanter...

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APA: Copy

Abbaspour Aghdam, F., KIANIMANESH, H.R., ARABIAN, D., & KHALILZADEH, R.. (2018). Design and Integration for Biodiesel Production from Vegetable Oil via Transesterification Reaction (Brief Report). JOURNAL OF AGRICULTURAL MACHINERY, 8(1 (15) ), 223-234. SID. https://sid.ir/paper/392292/en

Vancouver: Copy

Abbaspour Aghdam F., KIANIMANESH H.R., ARABIAN D., KHALILZADEH R.. Design and Integration for Biodiesel Production from Vegetable Oil via Transesterification Reaction (Brief Report). JOURNAL OF AGRICULTURAL MACHINERY[Internet]. 2018;8(1 (15) ):223-234. Available from: https://sid.ir/paper/392292/en

IEEE: Copy

F. Abbaspour Aghdam, H.R. KIANIMANESH, D. ARABIAN, and R. KHALILZADEH, “Design and Integration for Biodiesel Production from Vegetable Oil via Transesterification Reaction (Brief Report),” JOURNAL OF AGRICULTURAL MACHINERY, vol. 8, no. 1 (15) , pp. 223–234, 2018, [Online]. Available: https://sid.ir/paper/392292/en

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