In situ solvent recovery by using hydrophobic/oleophilic filter during wet lipid extraction from microalgae

2019 ◽  
Vol 42 (9) ◽  
pp. 1447-1455 ◽  
Author(s):  
Hogi Kim ◽  
Jihye Shin ◽  
Donghyo Lee ◽  
Sung Gap Im ◽  
Yong Keun Chang
RSC Advances ◽  
2021 ◽  
Vol 11 (35) ◽  
pp. 21207-21215
Author(s):  
Paidi Murali Krishna ◽  
Veerababu Polisetti ◽  
Krishnaiah Damarla ◽  
Subir Kumar Mandal ◽  
Arvind Kumar

In this study, a water-miscible ionic liquid (IL), 1-ethyl-3-methylimidazoliumacetate ([EMIM][Ac]), has been used for lipid extraction from marine diatoms Thalassiosira lundiana CSIR-CSMCRI 001 by following a non-polar solvent partition method.


2017 ◽  
Vol 21 ◽  
pp. 27-34 ◽  
Author(s):  
Emilie Angles ◽  
Pascal Jaouen ◽  
Jérémy Pruvost ◽  
Luc Marchal

2021 ◽  
Vol 16 (4) ◽  
pp. 733-743
Author(s):  
Alia Tasnim Hazmi ◽  
Farah B. Ahmad ◽  
Ahdyat Zain Athoillah ◽  
Ahmad Tariq Jameel

Microbial biodiesel is converted from microbial lipids via transesterification process. Most microbial biodiesel studies are focusing on the use of microalgal lipids as feedstock. Apart from using microalgae for lipid biosynthesis, lipids can also be extracted from other oleaginous microorganisms like fungi and yeast. However, there are gaps in the studies of lipid production from filamentous fungi, especially in-situ transesterification process. The aim of this project is to compare in-situ with the ex-situ transesterification of fungal biomass from Aspergillus oryzae. In ex-situ transesterification, two methods of lipid extraction, the Soxhlet extraction and the Bligh and Dyer extraction, were performed. For in-situ transesterification, two methods using different catalysts were investigated. Base-catalyzed in-situ transesterification of fungal biomass resulted on the highest Fatty Acid Methyl Esters (FAME) yield. The base-catalyzed in-situ transesterification was further optimized via Central Composite Design (CCD) of Response Surface Methodology (RSM). The parameters investigated were the catalyst loading, methanol to biomass ratio and reaction time. The optimization showed that the highest FAME yield was at 25.1% (w/w) with 10 minutes reaction time, 5% catalyst and 360:1 of the ratio of the methanol to biomass. Based on Analysis of Variance (ANOVA), the model was found to be significant according to the value of “Prob >F” of 0.0028. Copyright © 2021 by Authors, Published by BCREC Group. This is an open access article under the CC BY-SA License (https://creativecommons.org/licenses/by-sa/4.0). 


2020 ◽  
Vol 146 ◽  
pp. 188-195 ◽  
Author(s):  
Alejandra Sánchez-Bayo ◽  
Daniel López-Chicharro ◽  
Victoria Morales ◽  
Juan José Espada ◽  
Daniel Puyol ◽  
...  

2015 ◽  
Vol 768 ◽  
pp. 520-525
Author(s):  
Fen Fen Zhu ◽  
Juan Juan Qi ◽  
Xiang Wei ◽  
Lu Yao Zhao ◽  
Yi Qun Xiong

To develop new clean energy has become an urgent task for many countries forced by the energy and environment crisis. To make biodiesel from sewage sludge is one of the solutions. In this study, biodiesel production from sewage sludge by in situ transesterification was discussed. The solvent is methanol and catalyst is sulfuric acid. In-situ transesterification, has many merits over conventional transesterification reaction such as it simply the procedure by skipping the step of lipid extraction and as a result cost can be saved. That is, the steps — sludge dissolved, lipid extraction and transesterification reactions — take place simultaneously. Methanol acts as an extraction solvent and as an esterification reagent as well. Experiments were conducted to determine the optimal parameters of in-situ transesterification for maximizing the yield of biodiesel, which are methanol to sludge mass ratio, acid concentration and temperature. The optimum synthesis condition was determined by orthogonal test L16 (43), and it was found that an optimum biodiesel yield can be obtained from sewage sludge by in-situ transesterification (16.6%) at methanol to sludge mass ratio 10:1(w/w), H2SO4 concentration 5% (v/v), and temperature 65°C. Temperature, H2SO4 concentration, and methanol to sludge mass ratio in sequence had significant influence on FAMEs yield. The FAMEs in the product were analyzed by GC-MS and the purity can be higher than 96%.


2021 ◽  
pp. 126110
Author(s):  
Wanniarachchige Paramitha Sandani ◽  
Malith Premaratne ◽  
Thilini U. Ariyadasa ◽  
Jagath Kumara Premachandra

2017 ◽  
Vol 10 (27) ◽  
pp. 1319-1327
Author(s):  
Angel Dario Gonzalez-Delgado ◽  
Andres Fernando Barajas-Solano ◽  
Yeimmy Yolima Peralta-Ruiz

Microalgae has recently been highlighted as source of valuable products including biofuel. The production process of biofuels from microalgae involves mass cultivation, harvesting, deep dewatering, lipid extraction and biofuel conversion. In this work, lipids from microalgae Navicula sp. were obtained using multifunctional process that consists of acid hydrolysis or cellular disruption, oil extraction and in situ transesterification. The effect of alcohol added to produce ethyl and methyl esters on lipid extraction efficiency was evaluated using methanol and ethanol in order to determine the most suitable route for obtaining the high values of lipids and total reducing sugar. The highest lipid extraction efficiency and total reducing sugar (7.72 % and 2.63 mg/ml, respectively) was obtained for methanol. The low lipid extraction efficiency of multifuctional process is due to transesterification of lipids that gradually released into the system. The formation of alkyl esters was confirmed by FTIR with an increase in carbonyl peak as the reaction progressed, thus muntifuctional process reduce cost of alkyl esters production by eliminating the step of lipid extraction by solvent.


SPE Journal ◽  
2011 ◽  
Vol 16 (01) ◽  
pp. 55-64 ◽  
Author(s):  
Jyotsna Sharma ◽  
Ian D. Gates

2016 ◽  
Vol 29 (1) ◽  
pp. 89-103 ◽  
Author(s):  
Hassan Nezammahalleh ◽  
Mohsen Nosrati ◽  
Faezeh Ghanati ◽  
Seyed Abbas Shojaosadati

Data in Brief ◽  
2019 ◽  
Vol 26 ◽  
pp. 104416 ◽  
Author(s):  
Ying Du ◽  
Veronika Cyprichová ◽  
Kevin Hoppe ◽  
Boelo Schuur ◽  
Wim Brilman

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