An apparatus and method for dehydrating a quantity of previously air popped corn so as to maintain its crunchiness includes a support ring having an upstanding continuous peripheral wall configured to nest atop an upper edge of a receptacle, the upstanding continuous peripheral wall being complementary to an open top of the receptacle and defining an interior area. A distribution conduit having a cylindrical configuration is coupled to an inner surface of the support ring and has opposed upstream and downstream ends defining a channel therebetween. The upstream and downstream ends are open and the distribution conduit has an elongate configuration and is oriented axially relative to the support ring. A blow-drying device may be releasably mounted in the upstream end of the distribution conduit for generating a heated air stream and blowing the generated heated air stream from the upstream to the downstream end when energized.

A honey processing apparatus that is configured to provide processing of a wax/honey emulsion so as to separate the honey from the wax and provide separate collection thereof. The present invention includes a vessel having a first chamber and a second chamber. The first chamber includes an interior volume having a heating fluid disposed therein. The second chamber is also disposed within the interior volume of the first chamber and wherein the heating fluid is surroundably present thereto. A coil is present within the second chamber and the coil is fluidly coupled with the heating fluid. A pump is operably coupled to the coil and is configured to provide closed-loop recirculation of the heating fluid within the coil so as to provide heating of the wax/honey emulsion in order to facilitate the separation thereof. A honey extraction tube coupled with the second chamber provides extraction of the honey.

A method for preparing cassava flour with a low content of cyanogenic glycosides is provided. The method includes: washing, peeling, and cutting newly harvested fresh cassava to obtain cassava pellets, cassava shreds, or a cassava pulp as a raw material. The method further includes the following steps: immersing the raw material in a solution containing cellulase and pectinase for 10-30 minutes, and then placing the raw material in warm water with a temperature of 35-50° C. and a pH value of 5.5-6.5 and ultrasonicating for 10-30 minutes at an ultrasonic frequency of 50-80 kHz, to obtain an ultrasonicated raw material; drying and pulverizing the ultrasonicated raw material to obtain cassava flour with a low content of cyanogenic glycosides, a cyanogenic glycoside content of the cassava flour is less than 15 mg/kg.

Process for the production legume meal having a moisture content between 2% and 15%. The process includes feeding a continuous flow of legume meal into a wet heat treatment reactor together with a continuous flow of water or aqueous solution, which is dispersed into minute droplets; discharge the wet legume meal and feeding it into a thermal dehydration and treatment reactor.

Suggested is a process for the production of a UHT milk with improved taste characteristics, comprising the following steps: (a) Providing a raw milk; (b) Separating the raw milk into a skimmed milk fraction and a cream fraction; (c) Microfiltration of the skimmed milk fraction, obtaining a casein-containing retentate R1 and a fine whey as permeate P1; (d) Ultrafiltration of the fine whey of step (c), obtaining a permeate P2 that is rich in lactose and minerals, and a protein-rich retentate R2; (e) Pasteurization of the retentate R2; (f) Mixing the cream fraction, the retentate R1 and the permeate P2, obtaining a mixed fraction M1; (g) Ultra-high temperature treatment of the mixed fraction M1 of step (f); and (h) Mixing the ultra-heat treated fraction M1 of step (g) with the pasteurized retentate R2 of step (e), obtaining the target product.

A process for preparing a ready-to-eat mature coconut in which coconuts are selected based on its flotation characteristics, higher floaters being more mature. An oval or circular groove is carved partially into the bottom of the coconut shell. The coconut is then sealed into a heat tolerant plastic bag in which it is cooked, then frozen. Pieces of coconut husk are roasted until they turn black, then boiled in water to obtain a vapor that condenses to a liquid extraction, which is added to the bag before sealing it. The sealed bag is then heated to obtain sweet coconut water, some separation of coconut meat from the coconut shell, and the expansion of the coconut water during the spraying of steam to slightly split the coconut shell along the carved groove whereby the tip of a spoon can be used to pry off the coconut shell.

Disclosed are processes for reducing the cooked flavor, sulfur odor, and brown color of milk products that have been subjected to ultra-high temperature (UHT) sterilization via the UHT sterilization of certain milk fractions separately.

An object of the invention is to provide a beer-taste fermented malt beverage with an alcohol concentration of less than 1% (v/v), which is excellent in robust feeling of drinking, excellent in sweetness in harmony with sourness, and has beer-like flavor. The means for solving the problems is a beer-taste fermented malt beverage containing a wort fermented liquid, having a genuine extract component of 3.5% (w/w) or more, and an alcohol concentration of less than 1% (v/v).

Provided is a supporting method of supporting production of a maple syrup liquid obtained by concentrating maple sap, the supporting method including: inputting initial supply liquid information including a sugar content and color information of a supply liquid that is maple sap before concentration; inputting concentration target information including a target sugar content of a concentrated liquid obtained by concentrating the maple sap; and outputting predicted color information indicating a color of the maple syrup liquid predicted based on the initial supply liquid information and the concentration target information.

The process of producing concentrated maple sap can include concentrating the maple sap using membrane filtration to a sugar content of approximately 30° Brix, circulating the maple through a maple sap passage of a membrane, wherein the membrane contains the maple sap in a vacuum cavity, and evaporating the water from the maple sap across the membrane into the cavity. The concentrated maple sap having a sugar content above 50° Brix.