Hybrid drying apparatus for high or medium viscosity materials
US-2018335257-A1 · Nov 22, 2018 · US
US11226155B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11226155-B2 |
| Application number | US-201414217103-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 17, 2014 |
| Priority date | Mar 15, 2013 |
| Publication date | Jan 18, 2022 |
| Grant date | Jan 18, 2022 |
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A multi-chamber dryer using adjustable conditioned air flow is disclosed. According to one embodiment, an apparatus includes a drying belt configured to receive a product to be dried on a first surface of the drying belt and a heat medium in contact with a second surface of the drying belt. The heat medium is configured to heat the product and is maintained at a pre-determined temperature. The apparatus further includes a manifold that is positioned above the drying belt, where the manifold includes one or more orifices that inject conditioned air laterally across a width of the drying belt to remove evaporated water from the product
Opening claim text (preview).
The invention claimed is: 1. An apparatus, comprising: a moving drying belt configured to receive a product to be dried on a first surface of the moving drying belt; a manifold that is positioned above the moving drying belt, wherein the manifold includes one or more orifices that inject conditioned air laterally across a width of the moving drying belt; one or more screens underneath the one or more orifices that extend beyond an edge of the moving drying belt to guide a flow of the conditioned air from the one or more orifices; a port for an air pressure gauge used to maintain a positive pressure of approximately 16 pascals within the apparatus relative to an atmospheric pressure preventing contaminants from entering the apparatus; and a drying chamber through which the moving drying belt passes, wherein the drying chamber has circulated water in contact with a second surface of the moving drying belt to heat the product, wherein a temperature of the circulated water is below the circulated water's boiling point, and wherein the one or more orifices are located inside the drying chamber. 2. The apparatus of claim 1 , wherein the manifold is parallel to a length of the moving drying belt, and wherein the manifold is adjacent to a first side of the moving drying belt. 3. The apparatus of claim 1 , further comprising one or more of a chiller, a solid absorbent, and a compressor to de-humidify air and provide the conditioned air. 4. The apparatus of claim 3 , further comprising a particulate air filter to filter the de-humidified air and provide the conditioned air. 5. The apparatus of claim 2 , further comprising a duct to discharge conditioned air, wherein the duct is parallel to the length of the moving drying belt and adjacent to a second side of the moving drying belt. 6. The apparatus of claim 1 , further comprising a cover that covers and provides an adjustable headspace above the moving drying belt, where the manifold is positioned between the cover and the moving drying belt. 7. The apparatus of claim 6 , wherein the drying chamber provides one or more of an independently controlled air velocity, an independently controlled humidity, an independently controlled water temperature, and an independently controlled air temperature. 8. The apparatus of claim 6 , wherein the cover includes multi-wall poly carbonate panels. 9. The apparatus of claim 1 , wherein the one or more orifices provide an incident angle of the injected conditioned air of at least 40 degrees from the first surface of the moving drying belt. 10. The apparatus of claim 1 , wherein the one or more orifices inject the conditioned air at one or more of a desired pressure and with a desired air volume based on one or more of a type of the product, a moisture content of the product, and a dryer configuration. 11. A method, comprising: placing a product to be dried on a first surface of a moving drying belt; drying the product by passing the product on the moving drying belt through a drying chamber; maintaining a positive pressure of approximately 16 pascals within the drying chamber relative to an atmospheric pressure preventing contaminants from entering the apparatus using an air pressure gauge in a port of the drying chamber; contacting a second surface of the moving drying belt with circulated water to heat the product, wherein a temperature of the circulated water is below the circulated water's boiling point; and injecting conditioned air through one or more orifices in a manifold, across one or more screens that extend beyond an edge of the moving drying belt, and laterally across a width of the moving drying belt to remove evaporated water from the dried product, wherein the one or more orifices are located inside the drying chamber. 12. The method of claim 11 , further comprising providing conditioned air by one or more of de-humidifying air, heating the de-humidified air, and filtering the heated air. 13. The method of claim 12 , wherein de-humidifying air is based on using one or more of a chiller, a solid absorbent, and a compressor. 14. The method of claim 12 , wherein filtering the heated air is based on using a particulate air filter. 15. The method of claim 11 , further comprising discharging the injected air using a duct, where in the duct is parallel to a length of the moving drying belt and adjacent to a side of the moving drying belt. 16. The method of claim 11 , further comprising adjusting a headspace between a cover and the moving drying belt to control a quantity of the injected conditioned air. 17. The method of claim 16 , further comprising independently controlling one or more of an air velocity, a humidity and an air temperature of the injected conditioned air within the drying chambers. 18. The method of claim 17 , wherein controlling the air velocity of the injected conditioned air comprised one or more of opening an orifice, closing the orifice, and varying an opening size of the orifice. 19. The method of claim 11 , further comprising providing an incident angle of the injected conditioned air through the one or more orifices of at least 40 degrees from the first surface of the moving drying belt. 20. The method of claim 11 , further comprising injecting the conditioned air at one or more of a desired pressure and with a desired air volume based on one or more of a type of the product, a moisture content of the product, and a dryer configuration.
Ducting arrangements from the source of air or other gases to the materials or objects being dried · CPC title
Floors, roofs, or bottoms; False bottoms · CPC title
the belts being all horizontal or slightly inclined (F26B17/08 takes precedence) · CPC title
the heat source being a heated surface {, e.g. a moving belt or conveyor}(F26B3/22 takes precedence) · CPC title
Mechanical Engineering · mapped topic
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