| Supercritical fluid extraction and pressurized liquid extraction processes applied to eicosapentaenoic acid-rich polar lipid recovery from the microalga Nannochloropsis sp |
|
| Obtaining highly pure EPA-rich lipids from dry and wet Nannochloropsis gaditana microalgal biomass using ethanol, hexane and acetone |
|
| Simultaneous extraction and fractionation of lipids from the microalga Nannochloropsis sp. for the production of EPA-rich polar lipid concentrates |
|
| Optimization of biodiesel production from wet microalgal biomass by direct transesterification using the surface response methodology |
|
| Extraction of microalgal lipids and the influence of polar lipids on biodiesel production by lipase-catalyzed transesterification |
|
| Biodiesel production from Nannochloropsis gaditana lipids through transesterification catalyzed by Rhizopus oryzae lipase |
|
| Fatty acid methyl ester production from wet microalgal biomass by lipase-catalyzed direct transesterification |
|
| Enzymatic production of biodiesel from nannochloropsis gaditana lipids: Influence of operational variables and polar lipid content |
|
| Biodiesel production from wet microalgal biomass by direct transesterification |
|
| Production of biodiesel from vegetable oil and microalgae by fatty acid extraction and enzymatic esterification |
|
| Extraction of free fatty acids from wet Nannochloropsis gaditana biomass for biodiesel production |
|
| Extraction of saponifiable lipids from wet microalgal biomass for biodiesel production |
|
| Concentration of docosahexaenoic acid (DHA) by selective alcoholysis catalyzed by lipases |
|
| Production of triacylglycerols rich in palmitic acid at sn-2 position by lipase-catalyzed acidolysis |
|
| Production of triacylglycerols rich in palmitic acid at position 2 as intermediates for the synthesis of human milk fat substitutes by enzymatic acidolysis |
|
| Biocatalysis: Towards ever greener biodiesel production |
|
| Production of structured triacylglycerols by acidolysis catalyzed by lipases immobilized in a packed bed reactor |
|
| Concentration of eicosapentaenoic acid by selective esterification using lipases |
|
| Screening of lipases for enzymatic concentration of ?-linolenic acid (GLA) from seed oils |
|
| Production of structured triacylglycerols in an immobilised lipase packed-bed reactor: Batch mode operation |
|
| Kinetics of lipase-catalysed interesterification of triolein and caprylic acid to produce structured lipids |
|
| Hexane reduces peroxidation of fatty acids during storage |
|
| Lipase-catalyzed esterification of glycerol and polyunsaturated fatty acids from fish and microalgae oils |
|
| Lipase-catalyzed esterification of glycerol and polyunsaturated fatty acids from fish and microalgae oils |
|
| Lipase-catalyzed esterification of glycerol and polyunsaturated fatty acids from fish and microalgae oils |
|
| Lipase-catalyzed esterification of glycerol and polyunsaturated fatty acids from fish and microalgae oils |
|
| Downstream processing and purification of eicosapentaenoic (20:5n-3) and arachidonic acids (20:4n-6) from the microalga Porphyridium cruentum |
|
| Synthesis of polyunsaturated fatty acid-enriched triglycerides by lipase-catalyzed esterification |
|
| Optimization of fatty acid extraction from Phaeodactylum tricornutum UTEX 640 biomass |
|
