Tube bundle heat exchanger
A tube bundle heat exchanger has tubes which are held at each side in tube plates or oval-tube collecting-tube plates and are connected to these in each case by means of a weld seam. The connection of the tubes to the inlet-side tube plate or oval-tube collecting-tube plate is formed in each case by means of a conical and/or trumpet-shaped transition piece. The cross section of the transition piece reduces as viewed in the gas flow direction in such a way that the inlet-side end, as viewed in the gas flow direction, of the transition piece is connected in a buttjoint to the tube plate or oval-tube collecting-tube plate. The inner and outer contours of the transition piece and of the welded connection region are formed without gaps and comers to the tube plate or oval tube collecting-tube plate and so as to be straight and/or with a radius, measured from the outer contour, of at least 5 mm.
1. A tube bundle heat exchanger comprising:
a gas inlet chamber adapted to receive a gas into the heat exchanger;
a gas outlet chamber adapted to emit the gas from the heat exchanger;
an inlet-side tube plate disposed proximate to the gas inlet chamber, the inlet-side tube plate having a substantially flat axially outward facing surface, the inlet-side tube plate having a plurality of inlet-openings that are coplanar with the axially outward facing surface;
an outlet-side tube plate disposed proximate to the gas outlet chamber, the outlet-side tube plate having a plurality of outlet-openings; and
a plurality of tubes, each of the plurality of tubes having an inlet end with a first circular cross sectional flow area having a first inside diameter and each of the plurality of tubes having an outlet end, each of the inlet-openings of the inlet-side tube plate being circular;
wherein the outlet end of each of the plurality of tubes is welded to a respective outlet-opening of the outlet-side tube plate;
a transition piece attached to at least one of the plurality of tubes, the transition piece comprising;
(i) a tubular segment having a first circular cross sectional flow opening and the first inside diameter, the tubular segment extending along a longitudinal axis of the transition piece, the tubular segment having an outlet-side end at the first cross sectional flow opening, the outlet-side end being welded to the inlet end of a respective one of the plurality of tubes;
(ii) an arcuate outlet-side transition segment extending from the tubular segment towards a respective one of the inlet-openings of the inlet-side tube plate, the outlet-side transition segment having an axially extending arcuate outlet-side inside surface and an axially extending arcuate outlet-side exterior surface, the axially extending arcuate outlet-side exterior surface having an outlet-side radius of curvature;
(iii) a conical transition segment extending from the arcuate outlet-side transition segment and expanding symmetrically away from the longitudinal axis and outwardly toward a respective one of the inlet-openings of the inlet-side tube plate;
(iv) an inlet-side transition segment having an axially extending arcuate inlet-side inside surface and an axially extending arcuate inlet-side exterior surface, the axially extending arcuate inlet-side exterior surface having an inlet-side radius of curvature, the arcuate inlet-side transition segment extending a length from the conical transition segment toward and welded to a respective one of the inlet-openings and the arcuate inlet-side transition segment having circular cross sections entirely along the length thereof and having a second circular cross sectional flow opening that is substantially coplanar with the axially outward facing surface the inlet-side tube plate and the second circular cross sectional flow opening having a second inside diameter that is greater than the first inside diameter of the first cross sectional flow opening; and
wherein each of the plurality of tubes and the transition piece provide fluid communication of the gas between the gas inlet chamber and the gas outlet chamber,
wherein the axially extending arcuate inlet-side inside surface and the axially extending arcuate inlet-side exterior surface are formed without gaps or corners to the inlet-side tube plate, and
further wherein the outlet-side radius of curvature is 20 mm and the inlet-side radius of curvature is 5 mm.
2. The tube bundle heat exchanger of claim 1 , wherein the arcuate outlet-side transition segment further comprises an outlet-side inner contour.
3. The tube bundle heat exchanger of claim 1 , wherein the inlet-side inner contour and the inlet-side outer contour being formed without gaps or corners to the inlet-side tube plate.
4. The tube bundle heat exchanger of claim 1 , wherein the inlet-side transition segment is welded to a respective one of the inlet-openings without gaps and corners.
5. The tube bundle heat exchanger of claim 1 ,
wherein the transition piece has a length that is 1.5 times the second inside diameter.
6. The tube bundle heat exchanger of claim 1 , wherein the second inside diameter is at least 1.2 times the first inside diameter.
7. A tube bundle heat exchanger comprising:
a gas inlet chamber adapted to receive a gas into the heat exchanger;
a gas outlet chamber adapted to emit the gas from the heat exchanger;
an inlet-side tube plate disposed proximate to the gas inlet chamber, the inlet-side tube plate having a substantially flat axially outward facing surface, the inlet-side tube plate having a plurality of inlet-openings that are coplanar with the axially outward facing surface;
an outlet-side tube plate disposed proximate to the gas outlet chamber, the outlet-side tube plate having a plurality of outlet-openings; and
a plurality of tubes, each of the plurality of tubes having an inlet end with a first circular cross sectional flow opening having a first inside diameter and each of the plurality of tubes having an outlet end, each of the inlet-openings of the inlet-side tube plate being circular;
wherein the outlet end of each of the plurality of tubes is welded to a respective outlet-opening of the outlet-side tube plate;
a transition piece attached to at least one of the plurality of tubes, the transition piece comprising:
(i) an arcuate outlet-side transition segment welded to the inlet end of a respective one of the plurality of tubes and extending toward a respective one of the inlet-openings of the inlet-side tube plate, the arcuate outlet-side transition segment having an axially extending arcuate outlet-side inside surface and an axially extending arcuate outlet-side exterior surface, the axially extending arcuate outlet-side exterior surface having an outlet-side radius of curvature;
(ii) a conical transition segment extending from the outlet-side transition segment and toward a respective one of the inlet-openings of the inlet-side tube plate;
(iii) an inlet-side transition segment having an axially extending arcuate inlet-side inside surface and an axially extending arcuate inlet-side exterior surface, the axially extending inlet-side exterior surface having an inlet-side radius of curvature, the arcuate inlet-side transition segment extending a length from the conical transition segment toward and welded to a respective one of the inlet-openings and the arcuate inlet-side transition segment having circular cross sections entirely along the length thereof and having a second circular cross sectional flow opening that is substantially coplanar with the axially outward facing surface of the inlet-side tube plate and the second circular cross sectional flow opening having a second inside diameter that is greater than the first inside diameter of the first cross sectional flow area, and outlet-side radius of curvature being greater than the first inlet-side radius of curvature; and
wherein each of the plurality of tubes and the transition piece provide fluid communication of the gas between the gas inlet chamber and the gas outlet chamber,
wherein the axially extending arcuate inlet-side inside surface and the axially extending arcuate inlet-side exterior surface are formed without gaps or corners to the inlet-side tube plate, and
further wherein the outlet-side radius of curvature is 20 mm and the inlet-side radius of curvature is 5 mm.
8. A method for using the tube bundle heat exchanger according to claim 7 , comprising:
introducing the gas to the conical transition segment from the inlet-side tube plate.
9. The tube bundle heat exchanger of claim 7 , wherein the inlet-side transition segment is welded to a respective one of the inlet-openings without gaps and corners.