Spiral wound heat exchanger system with central pipe feeder

Abstract

The invention relates to a heat exchanger system comprising a jacket extending along a longitudinal axis and surrounding a jacket space. A pipe bundle is arranged in the jacket space wherein pipes are wound helically around a central pipe. At least one pre-distributor container is arranged in the jacket space for accommodating and degassing a liquid-gas mixture and designed to coat a distributing means with liquid degassed in the at least one pre-distributor container. The distributing means is designed to deliver the liquid to the pipe bundle. At the top the jacket has an inlet which is aligned with the longitudinal axis and in fluid connection with the central pipe. The central pipe has at least one lateral opening so that the liquid-gas mixture can be fed via the inlet, the central pipe, and the at least one lateral opening into the at least one pre-distributor container.

Claims

1. A heat exchanger system comprising: a jacket that extends along a longitudinal axis (L) and surrounds a jacket space (M) of the heat exchanger system (1), a pipe bundle (R) arranged within the jacket space (M) comprising a plurality of pipes (70) that are wound helically around a central pipe (10), wherein said central pipe (10) extends along said longitudinal axis (L), at least one pre-distributor container (50) arranged within said jacket space (M) for accommodating and degassing a liquid-gas mixture (F), said at least one pre-distributor container (50) is designed to degas liquid (F) from a liquid-gas mixture (F) and to distribute liquid (F) into a main distributor (60) for distributing liquid (F) onto said pipe bundle (R), an inlet (30) in the jacket (20) at the top (2) of the heat exchanger system (1) wherein said inlet is aligned with said longitudinal axis (L) and is in the form of an inlet nozzle (30), and wherein said inlet (30) is in fluid connection with said central pipe (10), said central pipe (10) has at least one lateral opening (100) that opens into the at least one pre-distributor container (50) whereby the liquid-gas mixture (F) is capable of flowing via said inlet (30), said central pipe (10), and said at least one lateral opening (100) into said at least one pre-distributor container (50).

2. The heat exchanger system according to claim 1, wherein said central pipe (10) has an end section (11) which is fixed on a tube plate (40) extending in a direction perpendicular to said longitudinal axis (L), wherein said tube plate (40) is provided at the top (2) of the heat exchanger system (1).

3. The heat exchanger system according to claim 2, wherein said tube plate (40) is connected at a circumferential edge area (41) thereof to said jacket (20).

4. The heat exchanger system according to claim 1, wherein said inlet nozzle (30) has an end section (31) which is fixed on a side of a tube plate (40) that faces away from said central pipe (10).

5. The heat exchanger system according to claim 1, wherein said central pipe (10) has a cylindrical wall (W) in which there is said at least one lateral opening (100).

6. The heat exchanger system according to claim 5, wherein said at least one pre-distributor container (50) originates from said cylindrical wall (W) and extends to an interior surface (20a) of said jacket (20).

7. The heat exchanger system according to claim 1, wherein said at least one pre-distributor container (50) has an upper edge (53), via which a gaseous phase (G) of the liquid-gas mixture (F) can flow downward into said jacket space (M), and said central pipe (10) has a cylindrical wall (W) in which there is said at least one lateral opening (100), wherein said upper edge (53) of said at least one pre-distributor container (50) is arranged above an upper edge (101) of said at least one lateral opening (100) of said central pipe (10).

8. The heat exchanger system according to claim 1, wherein said at least one pre-distributor container (50) is flow-connected to said main distributor (60) via at least one drain pipe (61) whereby degassed liquid (F) can flow from said at least one pre-distributor container (50) to said main distributor (60).

9. The heat exchanger system according to claim 1, wherein a perforated disk (102) is arranged in the at least one pre-distributor container (50), and said central pipe (10) has a cylindrical wall (W) in which there is said at least one lateral opening (100), wherein perforated disk (102) is positioned above said at least one lateral opening (100), so that a gaseous phase (G) of the liquid-gas mixture (F) can flow upward through said perforated disk (102), and wherein said perforated disk (102) is flow-connected to said main distributor (60) via at least one drain pipe (62) in said perforated disk (102) and at least one drain pipe (61) on the bottom (52) of the at least one pre-distributor container (50) which is aligned with via at least one drain pipe (62) in said perforated disk (102), whereby liquid (F) that is entrained by gaseous phase (G) and that drops onto said perforated disk (102), is capable of being introduced via said at least one drain pipe (62) of said perforated disk (102) into said at least one pre-distributor container (50) and then, via said at least one drain pipe (61) on the bottom (52) of said at least one pre-distributor container (50), into said main distributor (60).

10. The heat exchanger system according to claim 1, wherein said central pipe (10) has a cylindrical wall (W) in which there is said at least one lateral opening (100), and said central pipe (10) is closed downward below said at least one lateral opening (100), by a bottom (12), which is arranged along the longitudinal axis (L), at the height of a bottom (52) of said at least one pre-distributor container (50).

11. The heat exchanger system according to claim 1, wherein said at least one pre-distributor container (50) is arranged at the top (2) of the heat exchanger system (1).

12. The heat exchanger system according to claim 1, wherein said system comprises a plurality of said pre-distributor containers (50) at the same height along said longitudinal axis, and wherein each of said pre-distributor containers (50) is in the shape of a pie slice.

13. The heat exchanger system according to claim 1, wherein between two adjacent pre-distributor containers (50), a gap (104) extends in the radial direction of the jacket (20), through which, in each case, pipes (70) of the pipe bundle (R) run in direction of the longitudinal axis (L) past said pre-distributor containers (50) upward into the top (2) of the heat exchanger system (1).

14. The heat exchanger according to claim 9, said wherein perforated disk (102) extends over the entire pre-distributor container cross-section.

15. A heat exchanger system comprising: a jacket that extends along a longitudinal axis (L) and surrounds a jacket space (M) of the heat exchanger system (1), a pipe bundle (R) arranged within the jacket space (M) comprising a plurality of pipes (70) that are wound helically around a central pipe (10), wherein said central pipe (10) extends along said longitudinal axis (L), at least one pre-distributor container (50) arranged within said jacket space (M) for accommodating and degassing a liquid-gas mixture (F), said at least one pre-distributor container (50) is designed to degas liquid (F) from a liquid-gas mixture (F) and to distribute liquid (F) into a main distributor (60) for distributing liquid (F) onto said pipe bundle (R), an inlet (30) in the jacket (20) at the top (2) of the heat exchanger system (1) wherein said inlet is aligned with said longitudinal axis (L) and is in the form of an inlet nozzle (30), and wherein said inlet (30) is in fluid connection with said central pipe (10), said central pipe (10) has at least one lateral opening (100) that opens into the at least one pre-distributor container (50) whereby the liquid-gas mixture (F) is capable of flowing via said inlet (30), said central pipe (10), and said at least one lateral opening (100) into said at least one pre-distributor container (50), wherein said system comprises a plurality of said pre-distributor containers (50) at the same height along said longitudinal axis, and wherein each of said pre-distributor containers (50) is in the shape of a pie slice.

16. The heat exchanger system according to claim 15, wherein between two adjacent pre-distributor containers (50), a gap (104) extends in the radial direction of the jacket (20), through which, in each case, pipes (70) of the pipe bundle (R) run in direction of the longitudinal axis (L) past said pre-distributor containers (50) upward into the top (2) of the heat exchanger system (1).

17. The heat exchanger system according to claim 15, wherein said central pipe (10) has an end section (11) which is fixed on a tube plate (40) extending in a direction perpendicular to said longitudinal axis (L), wherein said tube plate (40) is provided at the top (2) of the heat exchanger system (1).

18. The heat exchanger system according to claim 17, wherein said tube plate (40) is connected at a circumferential edge area (41) thereof to said jacket (20).

19. The heat exchanger system according to claim 1, wherein each of said pre-distributor containers (50) is flow-connected to said main distributor (60) via at least one drain pipe (61) whereby degassed liquid (F) can flow from said at least one pre-distributor container (50) to said main distributor (60).

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The heat exchanger system according to the invention and further advantageous embodiments of the same will be described in more detail hereinafter with reference to the figures wherein:

(2) FIG. 1 shows a fragmentary, diagrammatic, sectional view of a heat exchanger system according to the invention; and

(3) FIG. 2 shows a top view of the pre-distributor container of the heat exchanger system according to FIG. 1.

(4) In connection with FIG. 2, FIG. 1 shows a heat exchanger system 1 according to the invention, with a pressurized jacket 20 that in sections is shaped like a hollow cylinder, which extends downward starting from a top 2 of the heat exchanger system 1 or jacket 20 along a longitudinal axis or cylindrical axis L, which runs parallel to the vertical, relative to a state of the heat exchanger system 1 that is arranged as directed.

(5) The jacket 20 surrounds a jacket space M of the heat exchanger system 1, in which a pipe bundle R is arranged, which is formed from a large number of pipes 70, which are wound helically around a central pipe 10 in several layers, which central pipe 10 is arranged concentric to the jacket 20 in the jacket space M, and whose longitudinal axis coincides with the longitudinal axis L of the jacket 20. The pipe bundle R serves to accommodate a fluid medium, which is to enter into indirect heat exchange with a liquid F that is to be run into the jacket space M, which liquid is released from above to the pipe bundle R.

(6) To this end, a distributing means 60 is arranged above the pipe bundle R, which is designed to distribute the liquid F to a cross-section of the jacket space M that runs perpendicular to the longitudinal axis L or to the vertical or to release the liquid F onto the pipe bundle R.

(7) In this case, the distributing means 60 is coated with the liquid F from one or more pre-distributor containers 50, which liquid results from the degassing and calming of a two-phase liquid-gas mixture F, which is to be accommodated in one or more pre-distributor containers 50.

(8) In this case, the liquid-gas mixture F is introduced at the top 2 of the jacket 20 or the heat exchanger system 1 in an inlet nozzle 30, aligned with the longitudinal axis L or the central pipe 10, in the heat exchanger system 1. Inlet nozzle 30 is positioned at a distance away from a tube plate 40, provided on the top 2. The inlet nozzle 30 is fixed to the tube plate via an end section 31. The tube plate 40 is connected to the jacket 20 via its circumferential edge area 41. On a side of the tube plate 40 facing away from the inlet nozzle 30namely in the jacket space Mthe wall W of the central pipe 10 with an end section 11 is fixed to the tube plate 40 and thus is anchored relative to the jacket 20. In this case, the central pipe 10, or the inside space I of the central pipe 10 that is surrounded by the wall W, is in fluid connection with the inlet nozzle 30 (via a corresponding opening in the tube plate 40), so that the liquid-gas mixture F that is introduced into the inlet nozzle 30 goes into the central pipe 10 or its inside space I and flows downward there. In this case, the liquid-gas mixture F introduced into the inside space I strikes a closure or bottom 12 of the central pipe 10, that runs perpendicular to the longitudinal axis L, and is directed into the pre-distributor container 50 by lateral openings 100 in the wall W of the central pipe 10.

(9) The pre-distributor containers 50 in each case extend, perpendicular to the longitudinal axis L, from a point starting from the wall W of the central pipe, i.e., in the radial direction of the central pipe 10, to the opposite interior surface 20a of the jacket 20 of the heat exchanger system 1. In this case, according to FIG. 2, the pre-distributor containers 50 are designed, in a cross-sectional plane running perpendicular to the longitudinal axis L, in the shape of pie slices, i.e., in the shape of circular sectors. Between two adjacent pre-distributor containers 50 a gap 104 extends in the radial direction of the jacket 20, through which, in each case, pipes 70 of the pipe bundle R run in direction of the longitudinal axis L past the pre-distributor containers 50 upward into the top 2 of the heat exchanger system 1. In each case, several pipes 70 are assembled at the ends of the pipes 70 to form a pipe rope, whereby such pipe ropes in the top 2 of the heat exchanger system 1 can be connected via the tube plate 40 to one assigned support each or laterally to the jacket 20 or tube plates with supports provided in the tube plate 40. The fixing of the pipes 70 in lateral tube plates has the drawback, however, that the pipes 70 must be bent radially outward. This would mean a higher production expense and thus longer manufacturing times. Moreover, a greater overall height would be necessary, which would lead to an increase in manufacturing costs. At the bottom or on the lower end of the heat exchanger system 1, the pipes 70 or pipe ropes formed therefrom are preferably also flow-connected to the supports provided on the jacket 20, so that fluid media can be introduced via the above-described supports into the pipe bundle R or can be drawn off from the pipe bundle R.

(10) The liquid-gas mixture F is accumulated, calmed, and degassed in the pre-distributor containers 50. The gaseous phase G can flow upward over an upper edge 53 of a side wall 51, originating from the bottom 52 of the respective pre-distributor container 50, in the jacket space M, and can flow downward through gaps 104. At the bottom 52 of the respective pre-distributor container 50, on a side, opposite to the opening 100 of the respective pre-distributor container 50, preferably two drain pipes 61 are provided, via which the degassed liquid F runs off into the distributing means 60.

(11) The upper edge 101 of the respective opening 100 in the wall W of the central pipe 10 is arranged along the longitudinal axis L below the upper edge 53 of the assigned pre-distributor container 50 as well as below a perforated disk 102, which extends into the respective pre-distributor container 50 via its cross-section and has a large number of holes 103. Gaseous phase G can flow through the holes 103 of the respective perforated disk 102 to even it out before gaseous phase G exits upward from the respective pre-distributor container 50. If liquid drops F are entrained by the gas flow, the latter can drop onto the respective perforated disk 102 and are in turn directed from there into the distributing means 60, namely via two drain pipes 62 in each of the respective perforated disk 102. In each case, a drain pipe 62 is aligned with an assigned drain pipe 61 that originates from the bottom 52 of the respective pre-distributor container 50. In FIG. 2, the pre-distributor container 50 that is on the right in the top view is shown without a corresponding perforated disk 102, so that the positions of the drain pipes 61 are visible on the bottom 52 of the pre-distributor container 50. This view also shows guide vanes for the 2-phase flow within the pre-distributor container 50.

(12) The bottoms 52 of the individual pre-distributor containers 50 run perpendicular to the longitudinal axis L at the height of the bottom 12 of the central pipe 10.

(13) Costly expansions of the top 2 of the spiral wound heat exchanger systems for separating gas and liquid can be avoided by the invention. Also, the overall height of the device can be reduced. In addition to the cost savings, this has the effect of shortening the pipe ropes. This facilitates manufacturing and in addition thus shortens the manufacturing time and reduces the costs of the device.

(14) Without further elaboration, it is believed that one skilled in the art can, using the preceding description, utilize the present invention to its fullest extent. The preceding preferred specific embodiments are, therefore, to be construed as merely illustrative, and not limitative of the remainder of the disclosure in any way whatsoever.

(15) The preceding examples can be repeated with similar success by substituting the generically or specifically described reactants and/or operating conditions of this invention for those used in the preceding examples.

(16) From the foregoing description, one skilled in the art can easily ascertain the essential characteristics of this invention and, without departing from the spirit and scope thereof, can make various changes and modifications of the invention to adapt it to various usages and conditions.

(17) The entire disclosures of all applications, patents and publications, cited herein and of corresponding European patent application EP 13003276.6, filed Jun. 27, 2013, are incorporated by reference herein.

(18) TABLE-US-00001 List of Reference Symbols 1 Heat Exchanger System 2 Top 10 Central Pipe 11 End Section 12 Bottom 20 Jacket 20a Interior 30 Inlet Nozzle 40 Tube Plate 41 Edge Area 50 Pre-Distributor Container 51 Side Wall 52 Bottom 53 Upper Edge 60 Distributing Means 61, 62 Drain Pipes 70 Pipe 100 Lateral Openings 101 Upper Edge 102 Perforated Disk 103 Holes 104 Gaps F Liquid .sup.F Liquid-Gas Mixture G Gas I Inside Space L Longitudinal Axis M Jacket Space R Pipe Bundle