Patent classifications
A23L3/375
METHOD FOR IN-LINE MEASUREMENT OF THE TEMPERATURE OF PRODUCTS TRAVELLING ON A CONVEYOR IN A FOOD PROCESSING OPERATION
Method for determining the temperature of products transported on the conveyor belt of a cryogenic tunnel, comprising the following steps: —continuously measuring the surface temperature of products travelling on the conveyor belt; —measuring the thickness of a product at the point where the temperature measurement is taken; —performing the following evaluation: a. when the thickness of the product is within a certain range, then the temperature measured for said product is considered to be a reliable value; b. when the thickness of the product is outside the range, then the last temperature value of the measured product is considered to be a reliable value according to paragraph a) above; c. after a determined period of time during which the measured thickness is outside the range, it is concluded that there are no products on the conveyor belt and the temperature measurements are no longer taken into account.
METHOD FOR IN-LINE MEASUREMENT OF THE TEMPERATURE OF PRODUCTS TRAVELLING ON A CONVEYOR IN A FOOD PROCESSING OPERATION
Method for determining the temperature of products transported on the conveyor belt of a cryogenic tunnel, comprising the following steps: —continuously measuring the surface temperature of products travelling on the conveyor belt; —measuring the thickness of a product at the point where the temperature measurement is taken; —performing the following evaluation: a. when the thickness of the product is within a certain range, then the temperature measured for said product is considered to be a reliable value; b. when the thickness of the product is outside the range, then the last temperature value of the measured product is considered to be a reliable value according to paragraph a) above; c. after a determined period of time during which the measured thickness is outside the range, it is concluded that there are no products on the conveyor belt and the temperature measurements are no longer taken into account.
SYSTEM FOR COOLING NON-LIQUID CONVEYABLE PRODUCT
Disclosed is a system for providing a desired amount of cooling to a quantity of non-liquid conveyable product in a vessel within a given length of residence time in the vessel, comprising:
(A) continuously feeding a mass of non-liquid conveyable product into a vessel, through the interior of the vessel, and out of the vessel, at a rate that provides a given predetermined length of residence time within the interior of the vessel, wherein the non-liquid conveyable product is moved through the interior of the vessel by engagement thereof with an impeller that is positioned in the interior of the vessel; and (B) feeding cryogen out of a plurality of nozzle openings directly into or onto the non-liquid conveyable product in the interior of the vessel while the impeller is moving the non-liquid conveyable product continuously past the nozzle openings, wherein the cryogen is fed into said non-liquid conveyable product from a sufficient number of said nozzle openings to provide the desired amount of cooling to the non-liquid conveyable product within the given period of residence time in the vessel, and wherein the flow of cryogen out of each nozzle opening is continuous or intermittent.
SYSTEM FOR COOLING NON-LIQUID CONVEYABLE PRODUCT
Disclosed is a system for providing a desired amount of cooling to a quantity of non-liquid conveyable product in a vessel within a given length of residence time in the vessel, comprising:
(A) continuously feeding a mass of non-liquid conveyable product into a vessel, through the interior of the vessel, and out of the vessel, at a rate that provides a given predetermined length of residence time within the interior of the vessel, wherein the non-liquid conveyable product is moved through the interior of the vessel by engagement thereof with an impeller that is positioned in the interior of the vessel; and (B) feeding cryogen out of a plurality of nozzle openings directly into or onto the non-liquid conveyable product in the interior of the vessel while the impeller is moving the non-liquid conveyable product continuously past the nozzle openings, wherein the cryogen is fed into said non-liquid conveyable product from a sufficient number of said nozzle openings to provide the desired amount of cooling to the non-liquid conveyable product within the given period of residence time in the vessel, and wherein the flow of cryogen out of each nozzle opening is continuous or intermittent.
METHOD FOR OPERATING A DOMESTIC REFRIGERATION APPLIANCE, IN WHICH A MISTING RATE IS ADAPTED, AND DOMESTIC REFRIGERATION APPLIANCE
A domestic refrigeration appliance has a separate storage area in an internal space into which foodstuffs, forming storage items, can be introduced. A liquid fluid can be introduced in the storage area independently of the internal space. For keeping the storage items fresh in the storage area a first operating mode and a storage mode, different therefrom, can be carried out. In the storage mode an aerosol mist generated by a misting device of the domestic refrigeration appliance is introduced as a fluid, and a misting rate of the aerosol mist during the storage mode is matched to a setpoint misting rate in dependence on at least one misting device-specific influencing parameter and/or a fluid-specific influencing parameter and/or a storage area-specific influencing parameter. There is also described a domestic refrigeration appliance.
Horizontal Axis Rotary Separation Apparatus and Process
A horizontal axis rotary separation apparatus is deployed in a process for separating resinous trichomes rich in flavoring, aromatic and/or medicinal components produced in plant trichome glands from unwanted plant matter. The process physically separates resin rich beads at the trichome gland head from extraneous plant matter by one or move separation sieves. The sieves are provided in or as a casing over a rigid frame member. The sieves are mesh fabric bags or screen that are easily opened and replenished in a batch operating mode, and are removable from the frame for cleaning and maintenance. Other aspects of the invention include processes that improve process efficiency and speed, and yield products of superior quality.
Energy-saving quick-freezing method for golden pomfret
The present invention provides an energy-saving quick-freezing method for golden pomfret. The method is putting golden pomfret into a liquid nitrogen quick-freezer with a cavity temperature of A, and when a core temperature of fish body reaches −6 to −4° C., turning off the liquid nitrogen quick-freezer; when the cavity temperature of the liquid nitrogen quick-freezer rises to B, starting the liquid nitrogen quick-freezer, and when the core temperature of the fish body reaches −19 to −17° C., turning off the liquid nitrogen quick-freezer; and taking out the golden pomfret and storing at −19 to −17° C.; wherein, the A is −105 to −85° C., the B is −95 to −65° C., and A<B.
Energy-saving quick-freezing method for golden pomfret
The present invention provides an energy-saving quick-freezing method for golden pomfret. The method is putting golden pomfret into a liquid nitrogen quick-freezer with a cavity temperature of A, and when a core temperature of fish body reaches −6 to −4° C., turning off the liquid nitrogen quick-freezer; when the cavity temperature of the liquid nitrogen quick-freezer rises to B, starting the liquid nitrogen quick-freezer, and when the core temperature of the fish body reaches −19 to −17° C., turning off the liquid nitrogen quick-freezer; and taking out the golden pomfret and storing at −19 to −17° C.; wherein, the A is −105 to −85° C., the B is −95 to −65° C., and A<B.
Liquid cryogen delivery and injection control apparatus
A delivery apparatus and method for delivering liquid cryogen to a chilling application includes a liquid cryogen feed tank; a liquid cryogen conduit in fluid communication between the feed tank and the application, wherein the feed tank is in fluid communication with a vessel which is in fluid communication with the conduit between the feed tank and the application; a weight measurement device for controlling the weight of liquid cryogen to be delivered to the application through the conduit; a flow controller for controlling the speed of delivery of the liquid cryogen to the application; wherein the application utilizes the liquid cryogen and produces an exhaust gas; a device for measuring the temperature of the exhaust gas, the device in operative communication with the flow controller; wherein the flow controller is configured to vary the speed of delivery of liquid cryogen from the vessel through the conduit in response to the temperature of the exhaust gas.
High-precision control system and method for shipborne cryogenic flash freezing of aquatic product using liquid nitrogen
A high-precision control system and method for shipborne cryogenic flash freezing of an aquatic product using liquid nitrogen is described. The system may include a main control system, a display unit, a liquid nitrogen supply system, a valve control unit, an acquisition unit, and a power unit. A flash freezing process is divided into four stages: a precooling stage, a flash freezing stage, a deep freezing stage, and a thermal insulation stage. Different cooling rates and flash freezing times are used for different stages, where a cooling rate is used in the flash freezing stage is the highest, a cooling rate used in the deep freezing stage is next, a cooling rate used in the precooling stage is the lowest, and an ambient temperature in a device is kept stable in the thermal insulation stage.