Provided is a processing apparatus for processing water-containing organic matters. The processing apparatus includes: a processing tank configured to store the water-containing organic matters; a stirring unit configured to stir the water-containing organic matters; a heater configured to heat the processing tank; an exhaust unit configured to exhaust gas from the processing tank at a rate from 1 m.sup.3/min to 300 m.sup.3/min; and an ion gas supply unit configured to supply ion gas into the processing tank with the exhaustion of the gas from the interior of the processing tank, the ion gas having an ion density of at least 2,000,000 pcs/cc, wherein the heater heats an interior of the processing tank while the stirring unit stirs the water-containing organic matters, and the ion gas is supplied into the processing tank according to the exhaustion by the exhaust unit, whereby processing the water-containing organic matters.

A material drying and cooling integrated machine, comprising a heating module, a drying module, a dust removal filter module, a temperature-lowering and dehumidifying module, and a cooling module. Dry hot air generated in the heating module can enter the drying module to dry materials; the temperature-lowering and dehumidifying module can conduct temperature lowering and dehumidification on air entering the interior thereof so as to form dry cold air, and the dry cold air can enter the cooling module to cool materials in the cooling module; the dry hot air enters the drying module to dry the materials in the drying module, then damp hot air is formed, and part of the damp hot air can be heated by the heating module again; the other part of the damp hot air can sequentially pass through the dust removal filter module and the temperature-lowering and dehumidifying module, and dry cold air can be formed.

Apparatus and methods for food production including a food preconditioner (228) operable to heat and partially pre-cook food ingredients, and a twin screw extruder (20) operable to further cook the preconditioned ingredients to create final food products. The extruder (20) includes a pair of hollow core extrusion screws (50, 52, 124, 126, 190) having elongated hollow core shafts (54, 128, 130, 192) equipped with helical fighting (56, 132, 134, 194) along the lengths thereof. The fighting (132, 134, 194) is also of hollow construction which communicates with the hollow core shafts (54, 128, 130, 192). The fighting (56, 132, 134, 194) also includes forward, reverse pitch sections (64, 162, 216). The extrusion screws (50, 52, 124, 126, 190) are designed to impart high levels of thermal energy into materials being processed in the extruders (20), without adding additional moisture.

Disclosed herein is a process for producing an animal feed having a defined nutritional profile from food waste. The process comprises accumulating successive batches of a plurality of food wastes that have been macerated and dehydrated, every batch of each of the plurality of food wastes having been sourced from the same one of a plurality of categorized producers of food waste and maintained separately at all times from others of the plurality of food wastes; independently mixing each of the accumulated batches of the macerated and dehydrated food wastes to produce a plurality of homogenized ingredients for an animal feed; analysing each of the homogenized ingredients to determine one or more nutritional parameters of the ingredient; and blending two or more of the homogenized ingredients to produce the animal feed having a defined nutritional profile.

A pet food cooker and mixer includes a housing within which is enclosed a motor and a removable mixing pot where the mixing pot is configured with curved walls and an open top, a longitudinal axis, and an outlet at one end. A mixer blade is driven by the motor and is configured with a shaft extending along the longitudinal axis within the mixing pot, the mixer blade comprising plurality of paddles extending radially from the shaft and configured to force food material toward the outlet and a scraper arm extending outward from the shaft, the scraper arm having a scraper paddle in contact with the curved walls. An extrusion auger is also driven by the motor and is configured to force food material through the outlet. The device is also configured with a heating element for heating the mixing pot.

A process to remove the glucosinolates of oilseed meals, such as Brassica carinata oilseed meals, is provided. In one embodiment, exogenous myrosinase is used to convert the glucosinolates to volatile isothiocyanate compounds, which can then be removed under conditions of mild heat and negative pressure. In another embodiment, heat and pressure are used to remove glucosinolates from Brassica carinata oilseed. The processed meals may contain less than 80% of their starting levels of glucosinolates and may be suitable for use in various applications, including as animal feeds.

Proposed is an offshore structure system, the offshore structure system comprising: a loader configured to load fish caught from a fishing vessel on an offshore structure; a classification sensor configured to classify the fish by type; a fishmeal producer configured to produce fishmeal from the first kind of fish classified by the classification sensor; a collagen producer configured to produce collagen from the second type of fish classified by the classification sensor; a dough maker configured to generate fish meat dough by adding additive to the fishmeal and the collagen; and a food producer configured to produce food by heating the fish meat dough.

The patent application describes a method of increasing bioavailability of animal feed comprising: hydrating a starting animal feed material with water to provide a hydrated animal feed material containing from 50 wt % to 99.99 wt % H.sub.2O; in a continuous-flow processing chamber, treating the hydrated animal feed material at a processing temperature selected from 40 C. to 90 C., a processing pressure (vacuum) selected from 5 psig to 14 psig, and a processing residence time selected from 1 minute to 60 minutes, thereby generating a processed animal feed material; and recovering the processed animal feed material as an enhanced-bioavailability animal feed. The enhanced-bioavailability animal feed has higher bioavailability compared to the starting animal feed material. Systems for increasing bioavailability of animal feed are also described and shown in drawings. Experimental examples are included, demonstrating significant enhancement of bioavailability using the disclosed technology, as measured by neutral detergent fiber digestibility at 12 hours.