Granted Patent B2

US 12,320,550 · App. 16/973,016 · Granted Jun 3, 2025

Inventors: Jun Kyu Park (Seoul, KR); Jun Gil Park (Seoul, KR)

Assignee: KYUNGDONG NAVIEN CO., LTD.

F24H8/00F24H1/0036F24H8/006F28D21/0007F28D2021/0024F28F1/325F28F13/08F28F2210/08

Abstract

Claims (57)

1. A heat exchanger unit comprising:

a sensible heat exchanging part disposed in a sensible heat exchange area configured to receive sensible heat generated by a combustion reaction and to heat water, the sensible heat exchanging part including a sensible heat exchange pipe configured to receive the water and allow the water to flow therethrough to form a sensible heat flow passage through which the water flows; and

a latent heat exchanging part disposed in a latent heat exchange area, the latent heat exchanging part including a latent heat exchange pipe configured to receive the water and allow the water to flow therethrough, wherein the latent heat exchange area is located downstream of the sensible heat exchange area based on a first reference direction that is a flow direction of combustion gas generated during the combustion reaction, the latent heat exchange area being configured to receive latent heat generated during a phase change of the combustion gas and to heat the water, and

a housing configured to surround the heat exchange areas to define the heat exchange areas therein,

wherein the latent heat exchange pipe includes a plurality of latent heat straight portions extending along a second reference direction perpendicular to the first reference direction, the plurality of latent heat straight portions being arranged to be spaced apart from each other along a third reference direction perpendicular to the first reference direction and the second reference direction and configured to form a latent heat flow passage through which the water flows and that is connected to the sensible heat flow passage,

wherein interior spaces of the sensible heat straight portions and the latent heat straight portions are formed to be long and narrow such that widths in the third reference direction are smaller than lengths in the first reference direction,

wherein the latent heat exchange pipe includes a plurality of upstream straight portions and a plurality of downstream straight portions located downstream of the upstream straight portions based on the first reference direction,

wherein the heat exchanger unit further comprises:

a sensible heat fin coupled with the sensible heat exchange pipe;

an upstream fin coupled to the upstream straight portions and arranged to be spaced apart from the sensible heat fin along the first reference direction; and

a downstream fin coupled to the downstream straight portions and arranged to be spaced apart from the upstream fin along the first reference direction,

wherein cross-sectional areas of the heat exchange areas defined on a plane perpendicular to the first reference direction are referred to as reference cross-sectional areas,

wherein most upstream side of each fin based on the first reference direction are referred to as an inlet end and the most downstream side of each fin based on the first reference direction are referred to as an outlet end and,

wherein the housing is provided such that the reference cross-sectional area decreases from the outlet end of the sensible heat fin to the inlet end of the upstream fin, and

wherein the housing is provided such that the reference cross-sectional area decreases from the outlet end of the upstream fin to the inlet end of the downstream fin along the first reference direction, and

wherein the housing is provided such that the reference cross-sectional area defined at the outlet end of the downstream fin is smaller than the reference cross-sectional area defined at the inlet end of the upstream fin.

2. The heat exchanger unit of claim 1 , wherein in cross-sections obtained by cutting the straight portions with a plane perpendicular to the second reference direction, perimeters of the straight portions are referred to as external dimensions of the straight portions,

wherein in the cross-sections obtained by cutting the straight portions with the plane perpendicular to the second reference direction, external dimensions of the straight portions from the most upstream sides of the straight portions to separation points of the combustion gas for the straight portions based on the first reference direction are referred to as contact lengths,

wherein values obtained by dividing the contact lengths of the latent heat straight portions by the external dimensions of the latent heat straight portions are greater than values obtained by dividing the contact lengths of the sensible heat straight portions by the external dimensions of the sensible heat straight portions, and

wherein the separation points are points at which a rate of change of speed of the combustion gas along the third reference direction on surfaces of the straight portions is 0.

3. The heat exchanger unit of claim 1 , wherein for the interior spaces of the latent heat straight portions, values obtained by dividing the widths in the third reference direction by the lengths in the first reference direction are referred to as aspect ratios, and

wherein the aspect ratios of the latent heat straight portions range from 0.05 to 0.3.

4. The heat exchanger unit of claim 1 ,

wherein the housing is provided such that based on the first reference direction, a reference cross-sectional area at the most downstream side is smaller than a reference cross-sectional area at the most upstream side.

5. The heat exchanger unit of claim 4 , wherein the plurality of latent heat straight portions form a plurality of rows,

wherein each row includes the latent heat straight portions located in the same position based on the first reference direction.

6. The heat exchanger unit of claim 1 , wherein the latent heat flow passage includes a parallel flow passage in at least a partial section.

7. The heat exchanger unit of claim 1 , wherein the sensible heat exchange pipe includes a plurality of sensible heat straight portions extending along the second reference direction, the plurality of sensible heat straight portions being arranged to be spaced apart from each other along the third direction and configured to form the sensible heat flow passage through which the water flows.

8. The heat exchanger unit of claim 7 , wherein for interior spaces of the straight portions, values obtained by dividing widths in the third reference direction by lengths in the first reference direction are referred to as aspect ratios, and

wherein the aspect ratios of the latent heat straight portions are smaller than the aspect ratios of the sensible heat straight portions.

9. The heat exchanger unit of claim 7 , wherein in cross-sections obtained by cutting the straight portions with a plane perpendicular to the second reference direction, perimeters of interior spaces of the straight portions are referred to as internal dimensions of the straight portions, and

wherein the internal dimensions of the latent heat straight portions are smaller than the internal dimensions of the sensible heat straight portions.

10. The heat exchanger unit of claim 7 , wherein in cross-sections obtained by cutting the straight portions with a plane perpendicular to the second reference direction, perimeters of interior spaces of the straight portions are referred to as internal dimensions of the straight portions,

wherein in the cross-sections obtained by cutting the straight portions with the plane perpendicular to the second reference direction, internal upstream portions and internal downstream portions adjacent to the most upstream sides and the most downstream sides of the interior spaces of the straight portions based on the first reference direction are formed in a shape of at least part of a sector having a predetermined radius of curvature, and pairs of internal lateral portions that are opposite sides of the interior spaces of the straight portions based on the third reference direction are formed in a shape of at least part of a sector having a radius of curvature different from the predetermined radius of curvature,

wherein in the cross-sections, lengths from the most upstream sides of the internal upstream portions to places where the internal downstream portions and the internal lateral portions meet based on the first reference direction are referred to as effective heat transfer lengths, and

wherein values obtained by dividing the effective heat transfer lengths of the latent heat straight portions by the internal dimensions of the latent heat straight portions are greater than values obtained by dividing the effective heat transfer lengths of the sensible heat straight portions by the internal dimensions of the sensible heat straight portions.

11. The heat exchanger unit of claim 10 , wherein the internal lateral portions of the latent heat straight portions have an infinite radius of curvature.

12. A condensing boiler comprising:

a burner assembly configured to cause a combustion reaction;

a combustion chamber located downstream of the burner assembly based on a first reference direction that is a flow direction of combustion gas generated during the combustion reaction, flame by the combustion reaction being located in the combustion chamber; and

a heat exchanger unit configured to receive sensible heat generated by the combustion reaction and the combustion gas and to heat water,

wherein the heat exchanger unit includes:

a sensible heat exchanging part disposed in a sensible heat exchange area configured to receive the sensible heat generated by the combustion reaction and to heat the water, the sensible heat exchanging part including a sensible heat exchange pipe configured to receive the water and allow the water to flow therethrough;

a latent heat exchanging part disposed in a latent heat exchange area, the latent heat exchanging part including a latent heat exchange pipe configured to receive the water and allow the water to flow therethrough, wherein the latent heat exchange area is located downstream of the sensible heat exchange area based on the first reference direction and is configured to receive latent heat generated during a phase change of the combustion gas and to heat the water; and

a housing configured to surround the heat exchange areas to define the heat exchange areas therein,

wherein the latent heat exchange pipe includes a plurality of latent heat straight portions extending along a second reference direction perpendicular to the first reference direction, the plurality of latent heat straight portions being arranged to be spaced apart from each other along a third reference direction perpendicular to the first reference direction and the second reference direction and configured to form a latent heat flow passage through which the water flows and that is connected to the sensible heat exchange pipe,

wherein interior spaces of the sensible heat straight portions and the latent heat straight portions are formed to be long and narrow such that widths in the third reference direction are smaller than lengths in the first reference direction,

wherein the latent heat exchange pipe includes a plurality of upstream straight portions and a plurality of downstream straight portions located downstream of the upstream straight portions based on the first reference direction,

wherein the heat exchanger unit further comprises:

a sensible heat fin coupled with the sensible heat exchange pipe;

an upstream fin coupled to the upstream straight portions and arranged to be spaced apart from the sensible heat fin along the first reference direction; and

a downstream fin coupled to the downstream straight portions and arranged to be spaced apart from the upstream fin along the first reference direction,

wherein cross-sectional areas of the heat exchange areas defined on a plane perpendicular to the first reference direction are referred to as reference cross-sectional areas,

wherein most upstream side of each fin based on the first reference direction are referred to as an inlet end and the most downstream side of each fin based on the first reference direction are referred to as an outlet end and,

wherein the housing is provided such that the reference cross-sectional area decreases from the outlet end of the sensible heat fin to the inlet end of the upstream fin, and

wherein the housing is provided such that the reference cross-sectional area decreases from the outlet end of the upstream fin to the inlet end of the downstream fin along the first reference direction, and

wherein the housing is provided such that the reference cross-sectional area defined at the outlet end of the downstream fin is smaller than the reference cross-sectional area defined at the inlet end of the upstream fin.

Assignments (1)

Priority Claims (5)

Continuity (1)

References Cited (176)