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.

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.

A microingredient feed additive dispensing apparatus and method for adding microingredients to animal feed are described. The apparatus includes a frame, a microingredient receptacle with a front portion and a rear portion, a receptacle mount that mounts the receptacle to the frame, a plurality of microingredient bins oriented above the receptacle, one or more empty-receptacle-detecting sensors arranged along the front portion of the receptacle, and a driver coupled to the receptacle to feed the microingredients toward and over an exit boundary of the receptacle. Microingredients are concurrently dispensed from bins into the receptacle. The amount of the microingredients dispensed from each microingredient bin is calculated and controlled. One or more empty-collection-feeder sensors determine whether and when the collection feeder is empty, without weighing the whole collection bin. The apparatus and method provide a more efficient and accurate way to add microingredients to animal feed.

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.

The present application is directed to a system and processing method for fractionating pre-formed forage hay bales into a fractionated leaf portion and a fractionated stem portion. More particularly, the system involves grinding, chopping and shredding bales, and fractionating the chopped and shredded bales using a shaker table and grate assembly, into a fractionated leaf portion and a fractionated stem portion using a shaker table. The resulting fractionated leaf portion and fractionated stem portion can then be further processed into pellets for animal feed products, or the fractionated stem portion can be re-baled. Pelletization includes customizing the size of the pellets and the addition of additives to the pellets according to customers specifications for customized animal feed products. Pellets derived from the fractionated leaf portion and the fractionated stem portion are then packaged, typically in bags, for storage and transport.

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.

This invention relates to a seaweed processing plant, more specifically a portable seaweed processing plant. The portable seaweed processing plant comprises a shipping container having a substantially rectangular cuboid shaped body with at least one releasably securable door to provide access to and from the interior of the container. The container is configured for transport on an articulated chassis. The shipping container houses a remotely monitored seaweed processing line including a seaweed washing station, a seaweed preprocessing station, a seaweed separation station to separate the seaweed into liquid seaweed and solid seaweed, and a seaweed packing station to pack the liquid seaweed and the solid seaweed for onward transport. In this way, the yield from the harvest is optimized, additional products are harvested, and the quality of the harvest is superior than would otherwise be the case.

This invention relates to a seaweed processing plant, more specifically a portable seaweed processing plant. The portable seaweed processing plant comprises a shipping container having a substantially rectangular cuboid shaped body with at least one releasably securable door to provide access to and from the interior of the container. The container is configured for transport on an articulated chassis. The shipping container houses a remotely monitored seaweed processing line including a seaweed washing station, a seaweed preprocessing station, a seaweed separation station to separate the seaweed into liquid seaweed and solid seaweed, and a seaweed packing station to pack the liquid seaweed and the solid seaweed for onward transport. In this way, the yield from the harvest is optimized, additional products are harvested, and the quality of the harvest is superior than would otherwise be the case.

The present disclosure relates in general to the imbibition of grains for the ruminant meat production and dairy production industries. More specifically, the present disclosure relates to systems and methods for maximizing the value of sprouted grains as a feedstuff for ruminant livestock using the combined applications of low volts of direct current and negative pressure during grain imbibition. The application of less than or equal to approximately 36.0 volts of direct current to grains in aqueous solutions for at least approximately 120 minutes, in addition to the application of negative pressure of approximately 10.0 inches of mercury (Hg) for at least approximately 60 minutes, have been found to mitigate harmful enteric carbon dioxide (CO.sub.2) and methane (CH.sub.4) emissions to offer opportunities for offset or inset carbon credit generation.