Method for determining stress levels in a material of a process engineering apparatus
US-2020173882-A1 · Jun 4, 2020 · US
US12013194B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12013194-B2 |
| Application number | US-201916397772-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 29, 2019 |
| Priority date | Apr 29, 2019 |
| Publication date | Jun 18, 2024 |
| Grant date | Jun 18, 2024 |
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A hot layer adapted for use in an asymmetric cross counter flow heat exchanger core that includes a number of alternating hot and cold layers, a hot inlet tent configured to receive a hot inlet flow and defining a hot inlet tent width, and a hot outlet tent configured to discharge a hot outlet flow and defining a hot outlet tent width. A hot inlet closure bar is located adjacent to the hot inlet tent, a hot outlet closure bar is located adjacent to the hot outlet tent, and two hot side closure bars are each located adjacent to respective corresponding inlet and outlet hot fins. An angle between the inlet fin direction and the middle fin direction ranges from 5-175 degrees, and the hot inlet tent width is less than the hot outlet tent width.
Opening claim text (preview).
The invention claimed is: 1. A hot layer adapted for use in an asymmetric cross counter flow heat exchanger core that includes a plurality of alternating hot and cold layers, the hot layer comprising: a plurality of inlet hot fins defining an inlet fin direction; a plurality of middle hot fins defining a middle fin direction; a plurality of outlet hot fins defining an outlet fin direction; a hot inlet closure bar on a first end of the hot layer and extending along the plurality of middle hot fins; a hot outlet closure bar on a second end of the hot layer and extending along the plurality of middle hot fins; a first hot side closure bar on a first side of the hot layer and disposed adjacent to the inlet hot fins; a second hot side closure bar on a second side of the hot layer and disposed adjacent to the outlet hot fins; a hot inlet on the first end of the hot layer and extending between the hot inlet closure bar and the first hot side closure bar and having a hot inlet width, wherein the hot inlet is configured to receive a hot inlet flow of a hot fluid that enters the hot layer at the hot inlet; and a hot outlet on the second end of the hot layer and extending between the hot outlet closure bar and the second hot side closure bar and having a hot outlet width, wherein the hot outlet is configured to discharge a hot outlet flow of a cooled hot fluid; wherein: an angle between the inlet fin direction and the middle fin direction ranges from 5-175 degrees; and the hot inlet width on the first end of the hot layer is less than the hot outlet width on the second end of the hot layer; a hot inlet closure bar width of the hot inlet closure bar is greater than a hot outlet closure bar width of the hot outlet closure bar; and the hot layer having a layer length in a direction of the inlet hot fins and a layer width in a direction that is perpendicular to the layer length, wherein a ratio of the hot inlet width on the first end of the hot layer to the layer width ranges from 5-50%, and wherein a ratio of the hot outlet width on the second end of the hot layer to the layer width ranges from 50-90%. 2. A heat exchanger core comprising the hot layer of claim 1 and at least one cold layer, each of the at least one cold layers including a cold closure bar located proximate the hot inlet. 3. The hot layer of claim 1 , wherein: the angle between the inlet fin direction and the middle fin direction is 90 degrees. 4. The hot layer of claim 1 , wherein the ratio of the hot inlet width to the layer width ranges from 25-40%. 5. The hot layer of claim 1 , wherein the ratio of the hot inlet width to the layer width ranges is 30%. 6. The hot layer of claim 1 , wherein: the hot layer defines a rectangular structure. 7. The hot layer of claim 1 , wherein the ratio of the hot outlet width to the layer width ranges from 65-80%. 8. The hot layer of claim 1 , wherein the ratio of the hot outlet width to the layer width is 75%. 9. The hot layer of claim 6 , wherein: the layer length ranges from 2.5-30 cm (1-12 inches); and the layer width ranges 2.5-30 cm (1-12 inches). 10. The hot layer of claim 6 , wherein: the layer length is greater than 30 cm (12 inches); or the layer width is greater than 30 cm (12 inches); or the layer length and layer width are both greater than 30 cm (12 inches). 11. The hot layer of claim 1 , further comprising a flow restrictor disposed near the hot outlet closure bar, configured to restrict flow through the inlet hot fins, the middle hot fins, and/or the outlet hot fins, thereby reducing a short-circuit of flow from the hot inlet to the hot outlet. 12. The hot layer of claim 11 , wherein the flow restrictor comprises a plate that is selected from the group consisting of a perforated plate and a partial height plate. 13. The hot layer of claim 11 , wherein the flow restrictor comprises a non-uniform fin configuration having of a variation in fin density and/or fin type. 14. The hot layer of claim 1 , wherein the inlet hot fins, middle hot fins, and outlet hot fins each comprise one or more of nickel, aluminum, titanium, copper, iron, cobalt, or alloys thereof. 15. The hot layer of claim 1 , wherein the inlet hot fins, middle hot fins, and outlet hot fins each comprise one or more of plastic, ceramic, or composite material. 16. The hot layer of claim 1 , wherein: the hot inlet flow comprises a hot gas; the hot gas defines a hot inlet flow temperature; and the hot inlet flow temperature ranges from 32 degrees F. (0 degrees C.) to 1,200 degrees F. (649 degrees C.). 17. An asymmetric cross counter flow heat exchanger, comprising the hot layer of claim 1 . 18. A hot layer adapted for use in an asymmetric cross counter flow heat exchanger core that includes a plurality of alternating hot and cold layers, the hot layer comprising: a plurality of inlet hot fins defining an inlet fin direction; a plurality of middle hot fins defining a middle fin direction; a plurality of outlet hot fins defining an outlet fin direction; a hot inlet closure bar on a first end of the hot layer and extending along the plurality of middle hot fins; a hot outlet closure bar on a second end of the hot layer and extending along the plurality of middle hot fins; a first hot side closure bar on a first side of the hot layer and disposed adjacent to the inlet hot fins; a second hot side closure bar on a second side of the hot layer and disposed adjacent to the outlet hot fins; a hot inlet on the first end of the hot layer and extending between the hot inlet closure bar and the first hot side closure bar and having a hot inlet width, wherein the hot inlet is configured to receive a hot inlet flow of a hot fluid that enters the hot layer at the hot inlet; and a hot outlet on the second end of the hot layer and extending between the hot outlet closure bar and the second hot side closure bar and having a hot outlet width, wherein the hot outlet is configured to discharge a hot outlet flow of a cooled hot fluid; wherein: the hot inlet width on the first end of the hot layer is less than the hot outlet width on the second end of the hot layer; a hot inlet closure bar width of the hot inlet closure bar is greater than a hot outlet closure bar width of the hot outlet closure bar; the hot layer having a layer width in a direction of the middle hot fins, wherein a ratio of the hot inlet width on the first end of the hot layer to the layer width ranges from 5-50%, and wherein a ratio of the hot outlet width on the second end of the hot layer to the layer width ranges from 50-90%; and an angle between the inlet fin direction and the middle fin direction is less than 90 degrees. 19. The hot layer of claim 18 , wherein the angle between the inlet fin direction and the middle fin direction ranges from 5-85 degrees. 20. A heat exchanger core comprising the hot layer of claim 18 and at least one cold layer, each of the at least one cold layers adapted for use with hot layer middle section.
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