Effects of Process Parameters on Hydrothermal Liquefaction of Microalgae Biomass Grown in Municipal Wastewater
- Authors: Arun J.1, Gopinath K.P.1, Shreekanth S.J.1, Sahana R.1, Raghavi M.S.1, Gnanaprakash D.1
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Affiliations:
- Department of Chemical Engineering, SSN College of Engineering, Rajiv Gandhi Salai (OMR)
- Issue: Vol 59, No 2 (2019)
- Pages: 194-200
- Section: Article
- URL: https://journals.rcsi.science/0965-5441/article/view/180749
- DOI: https://doi.org/10.1134/S0965544119020026
- ID: 180749
Cite item
Abstract
The emerging fuel crisis necessitates a shift in focus towards alternative renewable forms, so that sustainable development can be achieved. Bio-oil is a promising alternative renewable source of energy which is a third generation bio-fuel. Algae are a popular candidate for bio-fuel production due to their high lipid contents, ease of cultivation and rapid growth rate. In this study, Hydrothermal liquefaction of Scenedesmus obliques biomass cultivated in photo-bio-reactor (PBR) from wastewater was studied. The influence of process parameters on the bio-oil yield and bio-oil upgrading was analysed. Different S. obliques biomass to water ratios (0.025, 0.05, 0.075 and 0.1 g/ml) were liquefied at diverse temperatures ranging from 200 to 340°C under 5 MPa N2 gas atmosphere. The influence of catalyst on bio-oil upgradation was studied at varying catalyst loading of the range 1–5 wt %. Bio-oil was analysed using Gas Chromatography Mass Spectroscopy (GC-MS) and Fourier Transform Infrared Spectroscopy (FTIR). Results showed a maximum bio-oil yield of 24.57 wt % at 300°C, 15 g/200 ml biomass load and 2.5 wt % NaOH at 60 min holding time. Also, it was found that the gas generated from liquefaction process contained 22 vol % Hydrogen gas, 18 vol % Carbon dioxide gas, 27 vol % Carbon monoxide gas, 22 vol % of methane gas and a small amount of other gaseous components (H2S). HTL bio-oil was upgraded and it resulted in 30.15 wt % yield with higher degree of C7−C21 range hydrocarbons in it.
About the authors
J. Arun
Department of Chemical Engineering, SSN College of Engineering, Rajiv Gandhi Salai (OMR)
Email: gnanaprakashd@ssn.edu.in
India, Kalavakkam, Tamil Nadu, Chennai, 603110
K. P. Gopinath
Department of Chemical Engineering, SSN College of Engineering, Rajiv Gandhi Salai (OMR)
Author for correspondence.
Email: gopinathkp@ssn.edu.in
India, Kalavakkam, Tamil Nadu, Chennai, 603110
S. J. Shreekanth
Department of Chemical Engineering, SSN College of Engineering, Rajiv Gandhi Salai (OMR)
Email: gnanaprakashd@ssn.edu.in
India, Kalavakkam, Tamil Nadu, Chennai, 603110
R. Sahana
Department of Chemical Engineering, SSN College of Engineering, Rajiv Gandhi Salai (OMR)
Email: gnanaprakashd@ssn.edu.in
India, Kalavakkam, Tamil Nadu, Chennai, 603110
M. S. Raghavi
Department of Chemical Engineering, SSN College of Engineering, Rajiv Gandhi Salai (OMR)
Email: gnanaprakashd@ssn.edu.in
India, Kalavakkam, Tamil Nadu, Chennai, 603110
D. Gnanaprakash
Department of Chemical Engineering, SSN College of Engineering, Rajiv Gandhi Salai (OMR)
Author for correspondence.
Email: gnanaprakashd@ssn.edu.in
India, Kalavakkam, Tamil Nadu, Chennai, 603110
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