A temperature controlled plant maceration and extraction system and method is provided comprising an extraction chamber, an end cap at an one end of the extraction chamber, and an inlet gas valve at a second end. A hollow temperature jacket is formed around the extraction chamber from the first wall and an outer wall defining a space there between that is sealed at the one end and second end. A frame having a first and second pass-through axle is provided, one each fixedly mounted on the jacket between the one end and second end of the extraction chamber. Wherein organic matter is introduced via the one end, a solvent is injected into the chamber at the inlet valve on the second end, the extraction chamber is then rotated about the axels enabling the solvent to repeatedly wash over the organic matter performing maceration of organic matter.

This invention is in the field of micro-organism and algal cell processing. The invention relates to a method of maximizing migration of micro-organism and/or algal cells to a solvent fraction while simultaneously displacing water in a separate fraction and subsequent extraction of hydrophobic products from the organisms. The invention further relates to a method of sequestration of protein from an aqueous phase to an organic solvent.

An oil recovery extraction system includes a feeding and weighing system to weigh fruit and feed the fruit to an oil recovery extractor; extraction rollers that perforate a surface of the fruit to allow oil to flow out from the surface into the emulsion extractor reservoir; and a fruit washing system to spray the fruit with potable water to wash oil remaining on the fruit after the fruit has left the oil emulsion extractor reservoir; wherein an oil-water emulsion from the oil emulsion extractor and an oil-water emulsion from the fruit washing system are combined into an oil-emulsion; and a process control system to measure and control operational parameters of the machine, including calculating a setpoint feed flow of the fruit, then measuring and controlling the feed flow of fruit based on the setpoint, and further calculating a setpoint flow of potable water, heavy phase, then measuring and controlling the flows.

Processes are disclosed for obtaining a lipid from a cell by lysing the cell to form a lysed cell composition, adding an acid to lower the pH of the lysed cell composition, and demulsify the lysed cell composition, and obtaining the lipid from the demulsified lysed cell composition. Also disclosed are lipids prepared by the processes of the present invention wherein the lipids have a particular anisidine value, peroxide value, and/or phosphorus content.

The present disclosure relates to methods, systems, and devices for efficiently extracting high quality oils and distillates, such as essential oils and hydrosols, from organic matter, such as plant matters. In some embodiments, organic matter comprises active chemical elements, which are used for therapeutic, medicinal, culinary, and industrial purposes.

Provided herein are systems and methods for the facile extraction and purification of oils from plant material, including cannabis and hemp. The systems and methods herein are versatile, and may utilize a wide range of solvents to extract oils from a variety of plant-based material. Further, the provided systems and methods are closed loop, reducing the loss solvent and decreasing the risk of safety concerns such as human exposure to solvent chemicals or explosion of volatiles. In some embodiments, the systems and methods remove impurities from the extracted oils, for example waxes or other precipitates, and provide a higher purity and higher quality extract.

Methods for recovering solvent from biomass are disclosed herein. In one example, the method can include exerting pressure on wetted plant material to force liquid solvent from the plant matter so the solvent can be collected for reuse. The method can also include flowing pressurized gas through the wetted plant matter, thereby forcing liquid solvent from the plant material so the solvent can be collected for reuse.

An extraction system comprises an extraction chamber having an end cap at an one end accepting organic matter and gas or liquid solvent. A collection vessel is attached below the extraction chamber, a viewing vessel is sealed at an acute angle to a sidewall of the collection vessel enabling visual inspection at the collection plate. A gas tank is connected to the extraction chamber introducing solvent and a frame supports chamber by axles fixedly mounted on opposite sides of the extraction chamber, said axles supported by the frame structure enabling free rotation of the chamber about the axles. After gas is introduced to the organic matter, the extraction chamber is rotated vigorously about the axis, the one end is then connected to the open upper end of the collection vessel, and a lipid yield is collected at the collection plate.

Refrigerated solvent is fed through a cooling jacket around an essential element extraction vessel. After circulating through the cooling jacket, the solvent is re-chilled and at least some of the solvent is passed into the extraction vessel, in which essential elements dissolve into the solvent. Downstream of the extraction vessel, after adsorbent media treatment, the extracted oil and solvent mixture is filtered, in a chilled state, through one or more filtration units. A filtration unit may be a system of vertically oriented filters of decreasing pore size sealed and insulated from the atmosphere. Pressurized gas is used to force the oil and solvent through the filters. Each filter stage has a removable lid, which provides convenient access for replacing the filter cartridge without disturbing the thermally insulated sidewalls of the filter stage.

The invention relates to a method of combined cell digestion and extraction of oil-containing seeds having an oil content of >30% by mass, wherein production of a slurry from the oilseeds and ethanol is followed by a combination cell digestion with a subsequent ethanolic extraction, wherein the smaller portion of the oil of the oilseed and the alcohol-soluble constituents present therein are dissolved in the ethanol in accordance with the dissolution capacity of the ethanol for the oil and the alcohol-soluble constituents, a greater portion of the oil is displaced from the seed cells by the ethanol, forming a free oil phase in the ethanol. The free oil phase is removed and, according to the invention, has semi-raffinate quality, reducing the complexity of refining as an advantage of the method of the invention.