Pipe bundle recuperator on a sintering furnace and thermal transfer method having a sintering furnace and having a pipe bundle recuperator
US-2016025413-A1 · Jan 28, 2016 · US
US12050065B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12050065-B2 |
| Application number | US-202017613593-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 26, 2020 |
| Priority date | May 28, 2019 |
| Publication date | Jul 30, 2024 |
| Grant date | Jul 30, 2024 |
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A tube-bundle heat exchanger includes built-in elements formed by deflection surfaces, windows and directing sections. The product flows in the outer chamber of a tube-bundle heat exchanger with an inlet and an outlet for the product and an inlet and an outlet for the heat carrier medium in the tubes. The deflection panels including the tube-bundle heat exchanger are modified such that they leave windows open and a directing section is attached on the inlet side and the outlet side of the deflection surface. These directing sections run parallel to the tube axes and cross one another. The flow is divided by the direction sections on the inlet side and directed to the windows in opposing directions, where it then exits on respective opposing sides of the outlet sections and is deflected.
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The invention claimed is: 1. A bundle heat exchanger for delivering or dissipating heat and simultaneous mixing of product flow, comprising: a bundle of at least two extended heat exchange elements; an outer chamber; an inlet opening; an outlet opening, an inlet and an outlet arranged such that a product flow in the outer chamber is capable of flowing from the inlet opening to the outlet opening; and at least two fixed assemblies each comprising: at least two partial deflection surfaces and at least two windows, each of the at least two windows disposed in one of the partial deflection surfaces or between the partial deflection surfaces, each of the at least two windows leading from an inlet side to an outlet side of the at least two partial deflection surfaces, each of the partial deflection surfaces for each of the at least two fixed assemblies including a first directing section and a second directing section that are parallel to the extended heat exchange elements, the first directing section attached on the inlet side of the at least two partial deflection surfaces and the second directing section attached on the outlet side of the at least two partial deflection surfaces, the at least two partial deflection surfaces each including at least one portion not provided with a window leading from the inlet side to the outlet side of the deflection surface, the at least one portion having one or more bores or openings for passage of the extended heat exchange elements according to spacing thereof in the bundle, and the first directing section on the inlet side and the second directing section on the outlet side crossing one another at an angle of 90°. 2. The bundle heat exchanger according to claim 1 , wherein the bundle heat exchanger has a circular cross section. 3. The bundle heat exchanger according to claim 1 , wherein an axial distance between successive ones of the deflection surfaces corresponds to a height of two directing sections of the first directing section and the second directing section with no distances between the two directing sections. 4. The bundle heat exchanger according to claim 1 , wherein the at least two windows are arranged on opposite sides of the first directing section or on opposite sides of the second directing section. 5. The bundle heat exchanger according to claim 1 , wherein: the at least two fixed assemblies include a first fixed assembly and a second fixed assembly, the deflection surfaces for the first and second fixed assemblies stand transversely to the extended heat exchange elements, and the deflection surfaces for the first and second fixed assemblies are arranged one behind an other in a flow direction, the windows of the deflection surface of the first fixed assembly alternate with the at least one portion of the deflection surface of the second fixed assembly not provided with windows, and the at least one portion of the deflection surface of the first fixed assembly not provided with windows alternates with the windows of the deflection surface of the second fixed assembly. 6. The bundle heat exchanger according to claim 5 , wherein: the deflection surfaces of the first and second fixed assemblies each include the first directing section and the second directing section, and the first directing section or the second directing section of the first fixed assembly crosses the first directing section or the second directing section of the second fixed assembly at an angle of 90°. 7. The bundle heat exchanger according to claim 1 , wherein a cross section of the bundle is divided into approximately equal-sized partial surfaces by the first and second directing sections of the assemblies. 8. The bundle heat exchanger according to claim 1 , wherein of at least one of the deflection surfaces, portions provided with the at least two windows and the at least one portion not provided with windows are approximately a same size. 9. The bundle heat exchanger according to claim 1 , wherein for at least one of the deflection surfaces, portions provided with the at least two windows leading from the inlet side to the outlet side are smaller than the at least one portion not provided with windows leading from the inlet side to the outlet side. 10. The bundle heat exchanger according to claim 1 , wherein for each of the first directing section and the second directing section of at least one of the at least two fixed assemblies, a height is at most 0.25 times an inner diameter of the at least one assembly. 11. A method comprising: operating the bundle heat exchanger according to claim 1 for heat transfer with viscous products. 12. A method comprising: operating the bundle heat exchanger according to claim 1 as a reactor in exothermic or endothermic reactions. 13. The bundle heat exchanger according to claim 1 , wherein a number of the first directing section and the second directing section is different on the inlet side and on the outlet side. 14. The bundle heat exchanger according to claim 1 , wherein a height of first directing section and the second directing section is different on the inlet side and on the outlet side.
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