| Obtaining eicosapentaenoic acid-enriched polar lipids from microalga Nannochloropsis sp. by lipase-catalysed hydrolysis |
|
| Supercritical fluid extraction and pressurized liquid extraction processes applied to eicosapentaenoic acid-rich polar lipid recovery from the microalga Nannochloropsis sp |
|
| Obtaining EPA-rich polar lipids from microalga Nannochloropsis sp. by silica-gel chromatography using non-toxic solvents |
|
| Optimization of the enzymatic synthesis of structured triacylglycerols rich in docosahexaenoic acid at sn-2 position by acidolysis of Aurantiochytrium limacinum SR21 oil and caprylic acid using response surface methodology |
|
| 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 |
|
| 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 |
|
| 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 eicosapentaenoic acid (EPA) by selective alcoholysis catalyzed by lipases |
|
| Concentration of docosahexaenoic acid (DHA) by selective alcoholysis catalyzed by lipases |
|
| Synthesis of 2-monoacylglycerols and structured triacylglycerols rich in polyunsaturated fatty acids by enzyme catalyzed reactions |
|
| Production of structured triacylglycerols rich in palmitic acid at sn-2 position and oleic acid at sn-1,3 positions as human milk fat substitutes by enzymatic acidolysis |
|
| Enzymatic production of human milk fat substitutes containing palmitic and docosahexaenoic acids at sn-2 position and oleic acid at sn-1,3 positions |
|
| 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 |
|
| Synthesis of 2-monoacylglycerols (2-MAG) by enzymatic alcoholysis of fish oils using different reactor types |
|
| Production of structured triacylglycerols by acidolysis catalyzed by lipases immobilized in a packed bed reactor |
|
| Synthesis of 2-monoacylglycerols rich in polyunsaturated fatty acids by ethanolysis of fish oil catalyzed by 1,3 specific lipases |
|
| Production of structured triacylglycerols (STAG) rich in docosahexaenoic acid (DHA) in position 2 by acidolysis of tuna oil catalyzed by lipases |
|
