Systems and methods for fractionating whole stillage from an ethanol production facility are provided. Whole stillage undergoes a separation of its liquid portion (thin stillage) from the solid portion (fiber cake). In some embodiments, the solids and liquids in whole stillage may be separated utilizing a screening centrifuge. The fiber cake may be dried to generate a high fiber animal feed. The thin stillage may be provided to a three-phase separator for separation into an oil emulsion, an aqueous clarified stillage, and a protein paste. The protein paste may be dried to generate a high protein animal feed with greater than about 45% protein content. The clarified thin stillage is condensed to yield a syrup with greater than around 60% solids. The oil emulsion is subjected to a pH adjustment to liberate the oil from the emulsion, which is then separated.

The invention relates to a method for the simultaneous production of a solid transformation product of the substrate and crude ethanol comprising the following steps: preparing a substrate from milled or flaked biomass comprising proteinaceous matter which originates from soya bean, rape seed, or mixtures thereof, optionally in further mixture with proteinaceous matter originating from fava beans, peas, sunflower seeds, lupine, cereals, and/or grasses, mixing said substrate with live yeast in a dry matter ratio of from 1:1 to 10,000:1 and adding water in an amount which provides a ratio of wet bulk density to dry bulk density from 0.60 to 1.45 in the resulting mixture; incubating said mixture for 1-48 hours at a temperature of about 20-60 C.; and separating crude ethanol and wet solid transformation product from said mixture; further comprising that the incubation is performed as a continuous plug-flow process in a vertical, non-agitated, closed incubation tank with inlet means for said mixture and additives and outlet means for the solid transformation product and crude ethanol. The invention further relates to the products of this method as well as uses thereof.

Disclosed are devices and methods for non-cryogenic vitrification of biological materials that include the steps of providing one or more capillary channels of which a first opening is operably in contact with a moisture containing vitrification mixture made of a biological material and a vitrification agent. The capillary absorbs and transports the moisture to the second opening through capillary action, and the moisture is subsequently evaporated into a surrounding low humidity atmosphere until the vitrification mixture enters into a vitrified state.

A hybrid drying apparatus including: a bed portion having a horizontally disposed top surface; an object-to-be-dried supplying portion configured to spread an object to be dried on the top surface of the bed portion; and a driving unit configured to rotate and drive the bed portion or the object-to-be-dried supplying portion, wherein the object to be dried supplied from the object-to-be-dried supplying portion is spread on the top surface of the bed portion while the bed portion or the object-to-be-dried supplying portion is rotated, and the top surface of the bed portion is heated in such a manner that a lower portion of the bed portion is primarily heated so that the bed portion is used to dry the object to be dried coated on the top surface of the bed portion by the object-to-be-dried supplying portion.

A cultivation bag assembly for the cultivation of microbes, fungi and other organisms includes a bag having first and second walls joined along side edges to define a bag interior for containing a food substrate and an organism to be cultivated. At least one of the first and second walls is constructed of a layer of water-vapor permeable material to allow the passage of water vapor therethrough. A bag wall overlay layer formed from gas impermeable layer is releasably coupled to the bag. The overlay layer overlays the layer of water-vapor permeable material to prevent the passage of gases therethrough. The bag wall overlay layer has an opening with a gas filter patch covering the opening to allow the passage of oxygen and carbon dioxide gases through the gas filter patch to and from ambient air to facilitate incubation of the organism within the interior of the bag. The bag wall overlay layer is removable from the bag to allow water vapor to pass through the layer of water-vapor permeable material to ambient air facilitate drying of the bag contents after incubation is complete.

A dry grind biochemical production process and system with front end milling method is provided for improving biochemical and/or by-product yields, such as oil and/or protein yields. In one example, the process includes grinding corn kernels into particles then mixing the corn particles with a liquid to produce a slurry including oil, protein, starch, fiber, germ, and grit. Thereafter, the slurry is subjected to a front end milling method, which includes separating the slurry into a solids portion, including fiber, grit, and germ, and a liquid portion, including oil, protein, and starch, then milling the separated solids portion to reduce the size of the germ and grit and release bound starch, oil, and protein from the solids portion. The starch is converted to sugar, and a biochemical is produced therefrom then recovered. Also, the fiber can be separated and recovered. Oil and protein may be separated and recovered as well.

Disclosed are devices and methods for non-cryogenic vitrification of biological materials that include the steps of providing one or more capillary channels of which a first opening is operably in contact with a moisture containing vitrification mixture made of a biological material and a vitrification agent. The capillary absorbs and transports the moisture to the second opening through capillary action, and the moisture is subsequently evaporated into a surrounding low humidity atmosphere until the vitrification mixture enters into a vitrified state.

An industrialized protein production system using carbon-containing industrial gas includes a bacteria preparation system, a raw gas purification system, a water purification system, a bacteria separation system and a protein preparation system, wherein the bacteria preparation system is respectively communicated with the raw gas purification system, the water purification system and the bacteria separation system, and the protein preparation system is communicated with the bacteria separation system. By purifying the raw gas and the raw water and removing impurities from the raw gas and competing bacteria in the raw water, excellent raw materials and environment are provided for bacterial reproduction, which enable the raw gas to have high-efficiency fermentation, thereby increasing the yield of proteins.

A method of producing a cell growth medium. The method includes cultivating microbial cells by gas fermentation to obtain a biomass slurry, concentrating the biomass slurry by separating and removing a liquid phase from a solid phase, homogenizing the concentrated biomass slurry with high pressure homogenization, wherein the microbial cells are at least partially degrading, treating the homogenized biomass slurry by adding at least one protease, and heating the treated biomass slurry.

Reference is made to the Identification of the Microorganism, with the identification reference given by the DEPOSITOR of SoF1, having the Accession number given by the INTERNATIONAL DEPOSITORY AUTHORITY of VTT E-193585, received on Jun. 11, 2019, (date of original deposit).

Methods and systems for manipulating varied biological recyclable streams to produce agricultural admixtures are herein described. The resulting agricultural admixtures can be used to enhance crop yield, or as an animal provender. Managing the sources of varied biological recyclable streams can afford agricultural admixtures with controlled properties.