A process to coagulate wasted eggs which includes an acidification step of the liquid egg, followed by a coagulation step using a heat exchanger, such as a scraped surface heat exchanger, and optionally a drying step. The obtained coagulated egg product has useful properties and can be used as animal food. The process allows the disposal of wasted eggs generated in the poultry and related industries and the production of a valuable by-product with high protein and fat content.

The invention consists of novel systems and methods for mixing and/or applying biologies including live biologies and/or any additive having therapeutic or growth promoting value with and/or to animal feed, thereby creating treated animal feed, and for delivering such treated animal feed to animals in need via a delivery system. The invention also provides a system and method to treat seed with biologies prior to or contemporaneously with packaging, storing, and/or planting.

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.

An apparatus and method for simulating the effects of dew are disclosed. The apparatus includes a moveable platform; a rotatable base, the rotatable base being connected to the platform; and a plurality of elongated rods for penetrating and spraying beneath the surface of a windrow. The rods radiate from a longitudinal axis of the rotatable base.

The present disclosure provides methods for processing pistachio shells based on cooled, e.g., cryogenic, grinding. In embodiments, such a method comprises grinding raw pistachio shells in a cooled compression milling system, e.g., a cryo-compression milling system, under conditions to provide ground pistachio shells having a D.sub.50 particle size in a range of from 10 μm to 600 μm. Animal nutrition products are also provided. In embodiments, an animal nutrition product configured to be ingested by an animal is provided, the animal nutrition product comprising ground pistachio shells having a D.sub.50 particle size in a range of from 10 μm to 600 μm.

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.

An manufacturing device for amino acid coordination complexes, containing a reaction mechanism including a paddle drying reaction kettle, a motor, a rotation shaft, and paddles; a wet-type dust collector; a vacuum pump, and an ozone generator; one end of the rotation shaft is connected to the motor; another end of the rotation shaft extends into the paddle drying reaction kettle; a plurality of paddles are disposed on an outer wall of the rotation shaft and are rotatable along with the rotation shaft; the paddle drying reaction kettle is connected to one end of a vacuum pump through a gas discharging pipe; another end of the vacuum pump is connected with the ozone generator; a middle part of the gas discharging pipe is connected with the wet-type dust collector; the wet-type dust collector has a first wet filter tank and a second filter tank.

An apparatus is configured to apply a treatment agent to an agricultural byproduct. The apparatus includes a fragmenting chamber where the agricultural byproduct is fragmented into particles. An initial amount of a treatment agent is applied to the byproduct in the fragmenting chamber. Particles of a desired size flow through a screen from the fragmenting chamber to a recovery zone. A second amount of the treatment agent is applied to the particles in the recovery zone. A regulator regulates the amount of the treatment agent applied to the particles in the fragmenting chamber and the amount of treatment agent applied in the in the recovery zone. The regulation may be based on one or more feedback mechanisms.

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.

An apparatus is configured to apply a treatment agent to an agricultural byproduct. The apparatus includes a fragmenting chamber where the agricultural byproduct is fragmented into particles. An initial amount of a treatment agent is applied to the byproduct in the fragmenting chamber. Particles of a desired size flow through a screen from the fragmenting chamber to a recovery zone. A second amount of the treatment agent is applied to the particles in the recovery zone. A regulator regulates the amount of the treatment agent applied to the particles in the fragmenting chamber and the amount of treatment agent applied in the in the recovery zone. The regulation may be based on one or more feedback mechanisms.