Comparison of Hexane, Methanol, and Their Mixtures as Solvents for Microalgae Lipid Extraction by Hydrodynamic Cavitation

Setyawan, Martomo and Jamilatun, Siti and Syafii, Muhammad Nufail and Pratama, Resyaldi (2020) Comparison of Hexane, Methanol, and Their Mixtures as Solvents for Microalgae Lipid Extraction by Hydrodynamic Cavitation. [Artikel Dosen] (Submitted)

[thumbnail of 6. CEK SIMILARITY-Comparison of Hexane, Methanol, and Their Mixtures as Solvents for icroalgae Lipid Extraction by Hydrodynamic Cavitation.pdf] Text
6. CEK SIMILARITY-Comparison of Hexane, Methanol, and Their Mixtures as Solvents for icroalgae Lipid Extraction by Hydrodynamic Cavitation.pdf

Download (2MB)
[thumbnail of Comparison of Hexane, Methanol, and Their Mixtures as Solvents for Microalgae Lipid Extraction by Hydrodynamic Cavitation.pdf] Text
Comparison of Hexane, Methanol, and Their Mixtures as Solvents for Microalgae Lipid Extraction by Hydrodynamic Cavitation.pdf

Download (2MB)
[thumbnail of PER REVIEW-Comparison of Hexane, Methanol, and Their Mixtures as Solvents for Microalgae Lipid Extraction by Hydrodynamic Cavitation.pdf] Text
PER REVIEW-Comparison of Hexane, Methanol, and Their Mixtures as Solvents for Microalgae Lipid Extraction by Hydrodynamic Cavitation.pdf

Download (665kB)

Abstract

The process of producing biodiesel from microalgae as an effort to solve energy problems is currently constrained by the negative energy balance, which requires more energy to produce than the heating value of biodiesel. The lipid extraction assisted by hydrodynamic cavitation requires less energy extraction than the heating value of biodiesel. The effort to increase the energy efficiency of the hydrodynamic cavitation extraction process is to find a solvent that has a low boiling point. This study aims to improve energy efficiency by using a solvent mixture of hexane and methanol, which has a low boiling point. The results showed that the methanol hexane mixture with a volume ratio of 4:1 gave the lowest mixture boiling point of 51.2 °C with a yield of 3.28% g lipid / g dry microalgae. The process
2 runs at a temperature of 30 °C with a driving pressure of 5 kg / cm ,
with an extraction energy requirement of 2 kJ/g of lipids. This process is feasible to be developed to produce biodiesel from microalgae with a positive energy balance.

Item Type: Artikel Dosen
Subjects: T Technology > TP Chemical technology
Divisi / Prodi: Faculty of Industrial Technology (Fakultas Teknologi Industri) > S1-Chemical Engineering (S1-Teknik Kimia)
Depositing User: Dr., MT Siti Jamilatun
Date Deposited: 20 Oct 2021 00:52
Last Modified: 07 Jul 2022 03:02
URI: http://eprints.uad.ac.id/id/eprint/29062

Actions (login required)

View Item View Item