Spiral wound heat exchanger system with central pipe feeder

Patent metadata

Field	Value
Publication number	US-10113802-B2
Application number	US-201414315875-A
Country	US
Kind code	B2
Filing date	Jun 26, 2014
Priority date	Jun 27, 2013
Publication date	Oct 30, 2018
Grant date	Oct 30, 2018

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.

First claim

The invention claimed is:

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 ( 20 a ) 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

Assignees

• Linde Ag

Inventors

• Steinbauer Manfred
• Reithmeier Helmut
• Kerber Christiane
• Hammerdinger Markus
• Spreemann Jurgen

Classifications

• F28D2021/0033

  for cryogenic applications · CPC title

• F25J2290/32

  Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers · CPC title

• F28F2265/18

  for removing contaminants, e.g. for degassing · CPC title

• F28D7/024

  the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration · CPC title

• F28F9/026

  with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits · CPC title