Patent application number | Description | Published |
20090162919 | METHODS FOR CONCENTRATING MICROALGAE - The present invention provides commercially viable, large-scale methods for concentrating microalgae with an average diameter of about 20 μm or less. The methods find use in concentrating microalgae with an average diameter of about 5 μm or less, for example, | 06-25-2009 |
20100183744 | Systems and methods for maintaining the dominance of nannochloropsis in an algae cultivation system - Systems and methods for maintaining the dominance of | 07-22-2010 |
20100196995 | Systems and methods for maintaining the dominance and increasing the biomass production of nannochloropsis in an algae cultivation system - Systems and methods for maintaining the dominance and increasing the biomass production of | 08-05-2010 |
20100260618 | Systems, Methods, and Media for Circulating Fluid in an Algae Cultivation Pond - Systems, methods and media for generating fluid flow in an algae cultivation pond are disclosed. Circulation of fluid in the algae cultivation pond is initiated via at least one jet. The circulation of fluid generates a velocity of fluid flow of at least ten centimeters per second in the algae cultivation pond. A head is provided to the at least one jet that overcomes a head loss associated with the velocity of fluid flow of at least ten centimeters per second in the algae cultivation pond. | 10-14-2010 |
20100261922 | Systems and Methods for Extracting Lipids from and Dehydrating Wet Algal Biomass - Exemplary methods include centrifuging a wet algal biomass to increase a solid content of the wet algal biomass to between approximately 10% and 40% to result in a centrifuged algal biomass, mixing the centrifuged algal biomass with an amphiphilic solvent to result in a mixture, heating the mixture to result in a dehydrated, defatted algal biomass, separating the amphiphilic solvent from the dehydrated, defatted algal biomass to result in amphiphilic solvent, water and lipids, evaporating the amphiphilic solvent from the water and the lipids, and separating the water from the lipids. The amphiphilic solvent may be selected from a group consisting of acetone, methanol, ethanol, isopropanol, butanone, dimethyl ether, and propionaldehyde. Other exemplary methods include filtering a wet algal biomass through a membrane to increase a solid content of the wet algal biomass to between approximately 10% and 40% to result in a filtered algal biomass. | 10-14-2010 |
20100314324 | Clarification of Suspensions - A clarification system may comprise a channel having an inlet and an outlet, a length, bottom, and a height sufficient to contain a liquid having a depth. The clarification system may include one or more gas injectors disposed within the channel, configured to inject gas bubbles into a suspension flowing in the channel. In some embodiments, at least one gas injector injects gas bubbles having average or median size that does not exceed 100 microns in diameter. Some gas injectors inject bubbles having mean size below 50 microns. Some gas injectors inject gas via the precipitation of gas bubbles from a supersaturated liquid including a dissolved gas. Certain embodiments may be configured to form a quiet zone, typically near the top of the flowing suspension, in which turbulence may be minimized or substantially eliminated. Certain systems include a plurality of gas injectors disposed at different lengths along the channel. | 12-16-2010 |
20100317088 | Systems and Methods for Extracting Lipids from Wet Algal Biomass - Presented herein are exemplary systems and methods for extracting lipids from a wet algal biomass. An exemplary method comprises lysing a wet algal biomass with an insoluble granular lysing agent to create a lysate, creating a lipid-rich phase in the lysate, and separating the lipid-rich phase from the lysate. An exemplary system comprises a lysing station for creating a lysate from a wet algal biomass and a separation station for creating and separating a lipid-rich phase from the lysate. According to further exemplary systems and methods, ultrasound may be used in place of or in addition to a lysing agent to lyse the wet algal biomass. | 12-16-2010 |
20100325948 | SYSTEMS, METHODS, AND MEDIA FOR CIRCULATING AND CARBONATING FLUID IN AN ALGAE CULTIVATION POND - Systems, methods and media for carbonation of fluid in an algae cultivation pond via the use of jets are disclosed. Carbon dioxide is provided to a pressurized fluid. A jet of carbonated fluid is generated from the pressurized fluid and the carbon dioxide. Circulation of the fluid in the algae cultivation pond is initiated via the jet of carbonated fluid. | 12-30-2010 |
20100327077 | Nozzles for Circulating Fluid in an Algae Cultivation Pond - A nozzle for generating fluid flow in an algae cultivation pond is disclosed. The nozzle includes a surface forming a smooth flow path from an inlet to an outlet. The surface corresponds to a monotonically decreasing function from the inlet to the outlet. A ratio of an inlet cross-sectional area to an outlet cross-sectional area is greater than sixteen. | 12-30-2010 |
20100330658 | SILICEOUS PARTICLES - Various aspects provide for extracting siliceous particles. Siliceous particles may include or be derived from diatoms. Certain embodiments provide for segregating suspensions into two or more segregation products. In some cases, a first product includes siliceous particles, and a second product may include hydrophobic species. Certain aspects provide for extracting non-siliceous biomass (e.g., lipids). | 12-30-2010 |
20110041386 | Extraction From Suspensions - A suspension may include an aqueous liquid and suspended particles. The particles may include a nonpolar and/or hydrophobic substance (e.g., a lipid) substantially contained within polar and/or hydrophilic exterior layers. A method for extracting the suspended lipids may include adding a nonpolar solvent to the suspension and disrupting the exterior layers to expose the lipids to the nonpolar solvent. In some cases, particles may also include interior hydrophilic portions (e.g., intracellular water), which may be exposed to the aqueous liquid via disruption of the exteriors. The mixture may be accelerated to segregate the mixture into first and second products. The first product may have a majority of the nonpolar and/or hydrophobic substances. The second product may have a majority of the polar substances. | 02-24-2011 |
20110072713 | Processing Lipids - A method for converting lipids to alkyl esters may include receiving a reactant comprising one or more lipids. In some cases, the reactant may include substantial amounts of polar lipids and/or free fatty acids. Some reactants may be derived from photosynthetic organisms, such as algae and/or diatoms. The reactant may be mixed with an alcohol and a catalyst to form a mixture. The mixture may be heated, for example, to a temperature between 50 and 350 degrees Celsius, including between 80 and 220 degrees Celsius. Pressure may be controlled to be between 1 and 200 bar, including between 10 and 100 bar. At least a portion of the reactant may be converted to one or more alkyl esters. A biofuel may include alkyl esters made from lipids according to various methods. | 03-31-2011 |
20110136212 | Backward-Facing Step - Systems, methods and media for carbonation of fluid in an algae cultivation pond via the use of backward-facing steps are disclosed. In a first aspect, a method for initiating carbonation of a fluid flow in an algae cultivation pond is disclosed. Fluid flow is initiated over a backward-facing step in the algae cultivation pond. A backflow region is generated in the fluid flow downstream of the backward-facing step. Carbon dioxide is provided to the backflow region. | 06-09-2011 |
20110196163 | Systems and Methods for Extracting Lipids from and Dehydrating Wet Algal Biomass - Exemplary methods include centrifuging a wet algal biomass to increase a solid content of the wet algal biomass to between approximately 10% and 40% to result in a centrifuged algal biomass, mixing the centrifuged algal biomass with an amphiphilic solvent to result in a mixture, heating the mixture to result in a dehydrated, defatted algal biomass, separating the amphiphilic solvent from the dehydrated, defatted algal biomass to result in amphiphilic solvent, water and lipids, evaporating the amphiphilic solvent from the water and the lipids, and separating the water from the lipids. The amphiphilic solvent may be selected from a group consisting of acetone, methanol, ethanol, isopropanol, butanone, dimethyl ether, and propionaldehyde. Other exemplary methods include filtering a wet algal biomass through a membrane to increase a solid content of the wet algal biomass to between approximately 10% and 40% to result in a filtered algal biomass. | 08-11-2011 |