F26B3/34

COOKING APPLIANCE WITH ELECTRICAL COOKING ELEMENT DRYING OPERATIONS
20220404024 · 2022-12-22 ·

A cooking appliance and method of operation thereof in which cooking element drying operations are implemented to drive moisture out of the electrically-insulative material in a sheathed electrical cooking element. In many instances, the cooking element drying operations are of relatively short duration and/or include multiple cycles to drive moisture out of the electrically-insulative material without generating sufficient leakage current to cause a GFCI trip, and in some instances, while maintaining a surface temperature of the cooking element below a temperature that could cause a skin burn to occur and/or for items in contact with the cooking element to be damaged.

COOKING APPLIANCE WITH ELECTRICAL COOKING ELEMENT DRYING OPERATIONS
20220404024 · 2022-12-22 ·

A cooking appliance and method of operation thereof in which cooking element drying operations are implemented to drive moisture out of the electrically-insulative material in a sheathed electrical cooking element. In many instances, the cooking element drying operations are of relatively short duration and/or include multiple cycles to drive moisture out of the electrically-insulative material without generating sufficient leakage current to cause a GFCI trip, and in some instances, while maintaining a surface temperature of the cooking element below a temperature that could cause a skin burn to occur and/or for items in contact with the cooking element to be damaged.

ELECTROHYDRODYNAMIC DRYING OF MOIST POROUS MATERIALS
20230088399 · 2023-03-23 ·

An electrohydrodynamic (EHD) drying apparatus includes a non-uniform electric field resulting from an electric field source operable for a high potential, and an electric field source operable for a low potential. A power source is connected to the electric field sources for producing the non uniform electric field for inducing dielectrophoresis (DEP) in an article within the uniform electric field. In particular configurations, the applied non-uniform electric field is for separating a vapor phase being formed during drying from the liquid phase. The electric field source defines a polarizer adapted to produce dielectrophoresis, and the electric field induces coupled electrostatics and momentum for disposing liquid towards the high electric field for drying.

Method for drying articles

A method for drying an article with a radio frequency (RF) applicator having anode elements and cathode elements includes capacitively coupling the anode elements, capacitively coupling the cathode elements, capacitively coupling an anode element to a cathode element, and energizing the RF applicator to generate an RF field between anode and cathode elements wherein liquid residing within the field will be dielectrically heated.

Method for drying articles

A method for drying an article with a radio frequency (RF) applicator having anode elements and cathode elements includes capacitively coupling the anode elements, capacitively coupling the cathode elements, capacitively coupling an anode element to a cathode element, and energizing the RF applicator to generate an RF field between anode and cathode elements wherein liquid residing within the field will be dielectrically heated.

Plant material drying methods

A method of drying fresh plant material wherein the fresh plant material containing a desired heat labile compound is exposed to microwave energy at an intensity and for a time sufficient to remove a majority of the water from the plant material without degrading a majority of the heat labile compound. The method is particularly suited to in-field drying of freshly harvested plant material to reduce the weight and volume of the plant material for savings transportation costs to an extraction facility while preserving at high levels the amount and activity of the desired heat labile compound.

Hybrid RF/conventional clothes dryer

The present application encompasses methods and apparatus for heating a load such as clothes immersed in a medium such as water during a heating period. A method embodiment of the present invention comprises heating the load and medium within an enclosure by subjecting said load and medium to heated air originated from a conventional energy source; and applying heat to said load and medium within the enclosure via an AC electrical field, embodied as a capacitor, originated from an RF power source.

Flavor Encapsulation Using Electrostatic Atomization

Disclosed is an electrostatic spray drying process for encapsulating a core material, such as a volatile flavor oil, within a carrier or wall material. The process is achieved by atomizing a liquid emulsion comprising the core material and the wall material, applying an electrostatic charge at the site of atomization, and drying the atomized emulsion into an encapsulated, free-flowing powder. Applying an electrostatic charge at the site of atomization allows the spray drying to be accomplished at significantly reduced temperatures, in particular, inlet temperatures in the range of 25° C. to 110° C., and outlet temperatures in the range of 25° C. to 80° C. The low drying temperatures impart improvements in the resulting encapsulated powdered product, including better retention of volatile flavor components, a flavor profile comparable to that of the starting liquid formulation, and better hydration and dissolution in water-based applications.

Flavor Encapsulation Using Electrostatic Atomization

Disclosed is an electrostatic spray drying process for encapsulating a core material, such as a volatile flavor oil, within a carrier or wall material. The process is achieved by atomizing a liquid emulsion comprising the core material and the wall material, applying an electrostatic charge at the site of atomization, and drying the atomized emulsion into an encapsulated, free-flowing powder. Applying an electrostatic charge at the site of atomization allows the spray drying to be accomplished at significantly reduced temperatures, in particular, inlet temperatures in the range of 25° C. to 110° C., and outlet temperatures in the range of 25° C. to 80° C. The low drying temperatures impart improvements in the resulting encapsulated powdered product, including better retention of volatile flavor components, a flavor profile comparable to that of the starting liquid formulation, and better hydration and dissolution in water-based applications.

Alignment film drying system and a method for drying alignment films

An alignment film drying system and a method for drying alignment films are proposed. The alignment film drying system is used for drying an alignment film coated on a substrate. The alignment film drying system includes a plurality of magnetrons. The alignment liquid is coated on one side of the substrate facing the plurality of magnetrons and is heated through electromagnetic radiation produced by the plurality of magnetrons. The dried alignment liquid forms an alignment film having a uniform thickness, which ensures that the display effect of LCDs is better.