Cooling tower with indirect heat exchanger

Patent metadata

Field	Value
Publication number	US-2016363376-A1
Application number	US-201514738132-A
Country	US
Kind code	A1
Filing date	Jun 12, 2015
Priority date	Oct 9, 2014
Publication date	Dec 15, 2016
Grant date	—

Abstract

A heat exchange apparatus is provided with an indirect evaporative heat exchange section. The indirect evaporative heat exchange section is comprised of a series of serpentine tubes, and an evaporative liquid is passed downwardly onto the indirect heat exchange section. The evaporative liquid is collected in a sump and then pumped upwardly to be distributed again across the indirect heat exchange section. An improved heat exchange apparatus is provided with an indirect evaporative heat exchange section consisting of a series of serpentine tubes comprised of tube runs both of normal and increased height between tube runs. A direct heat exchange section may be provided in the increased vertical spacing between tube runs.

First claim

What is claimed is:

1 . A method of exchanging heat comprising the steps of:
providing an indirect evaporative heat exchange section, the indirect heat exchange section conducting a fluid stream within a plurality of pathways, the indirect heat exchange section comprising a top and a bottom, distributing an evaporative liquid generally downward onto and through the indirect heat exchange section such that indirect heat exchange occurs between the fluid stream within the plurality of pathways and the evaporative liquid, moving air through the indirect section, the air moving through the indirect heat exchange section exchanging heat with the evaporative liquid moving through the indirect heat exchange section and hence indirectly exchanging heat with the fluid stream within the plurality of pathways in the indirect section, wherein the indirect heat exchange section is comprised of a series of serpentine tubes comprising run sections and vertically spaced apart return bend sections, the series of serpentine tubes including at least one area having an increased vertical spacing between vertically adjacent run sections of the serpentine tubes, such increased vertical spacing formed by the vertically spaced apart return bend sections, and providing a direct heat exchange section in one or more of the areas in the indirect heat exchange section having increased vertical spacing between vertically adjacent run sections of the series of serpentine tubes.

2 . The method of exchanging heat of claim 1 , further comprising:
collecting substantially all of the evaporative liquid that exits the indirect heat exchange section, and pumping the collected evaporative liquid upwardly such that the collected evaporative liquid can be distributed generally downward onto and through the indirect heat exchange section.

3 . The method of exchanging heat of claim 1 wherein
the air moving through the indirect heat exchange section moves generally counter-current to the direction of flow of the evaporative liquid through the indirect heat exchange section.

4 . The method of exchanging heat of claim 1 wherein
the air moving through the indirect heat exchange section moves generally cross-current to the direction of flow of the evaporative liquid through the indirect heat exchange section.

5 . The method of exchanging heat of claim 1 wherein
the direct heat exchange section comprises a fill assembly located in one of the areas in the indirect heat exchange section having increased vertical spacing between vertically adjacent run sections of the series of serpentine tubes.

6 . The method of exchanging heat of claim 1 further comprising:
a support frame whereby the direct heat exchange section is supported such that it does not contact the indirect heat exchange section.

7 . The method of exchanging heat of claim 1 further comprising:
the direct heat exchange section is supported by being in contact with the indirect heat exchange section.

8 . The method of exchanging heat of claim 1 wherein the increased vertical spacing between tube runs comprises: one 90 degree bend, one vertical length of tube run followed by another 90 degree bend.

9 . The method of exchanging heat of claim 1 wherein the increased vertical spacing between tube runs forms a generally rectangular shape.

10 . The method of exchanging heat of claim 1 wherein the increased vertical spacing between tube runs forms a generally triangular shape.

11 . The method of exchanging heat of claim 1 wherein the direct section evaporates evaporative liquid at a rate of 110% to 400% more than that in the indirect section.

12 . The method of exchanging heat of claim 1 wherein
the increased vertical spacing formed by the vertically spaced apart return bend sections is about 12 inches (30.48 cm).

13 . The method of exchanging heat of claim 1 wherein
the increased vertical spacing formed by the vertically spaced apart return bend sections is from 2 inches (5.08 cm) to 60 inches (152.4 cm).

14 . The method of exchanging heat of claim 1 wherein
the direct heat exchange section is comprised of generally rectangular fill sheets.

15 . The method of exchanging heat of claim 1 wherein
the direct heat exchange section is comprised of generally triangular fill sheets.

16 . The method of exchanging heat of claim 1 wherein
the increased vertical spacing formed by the vertically spaced apart return bend sections is at least 2 inches (5.08 cm).

17 . The method of exchanging heat of claim 1 wherein
the direct heat exchange section is comprised of removable fill sheet sections.

18 . The method of exchanging heat of claim 1 wherein the airflow is operable between 0 to 100% flow rate.

19 . The method of exchanging heat of claim 1 wherein the same top and bottom indirect heat exchanger are connected with vertical runs between two 90 degree elbows

20 . A method of exchanging heat comprising the steps of:
providing an indirect heat exchange section, the indirect heat exchange section conducting a fluid stream within a plurality of pathways, the indirect heat exchange section comprising a top and a bottom, moving air through the indirect section, the air moving through the indirect heat exchange section exchanging heat with the fluid stream within the plurality of pathways in the indirect section, wherein the indirect heat exchange section is comprised of a serpentine coil assembly comprised of a series of serpentine tubes comprising run sections and return bend sections, certain of the return bend sections having a greater vertical spacing than other of the return bend sections, the serpentine coil assembly including at least one area having an increased vertical spacing between vertically adjacent run sections, such increased vertical spacing formed by the return bend sections having a greater vertical spacing, an inlet header and an outlet header operatively connected to the series of serpentine tubes such that the fluid stream can pass into the series of serpentine tubes and out from the series of serpentine tubes, and providing a direct heat exchange section in one or more of the areas in the indirect heat exchange sections having increased vertical spacing between vertically adjacent run sections of the series of serpentine tubes.

21 . The method of exchanging heat of claim 20 wherein
the direct heat exchange section comprises a fill assembly located in one of the areas in the indirect heat exchange section having increased vertical spacing between vertically adjacent run sections of the series of serpentine tubes.

22 . A method of exchanging heat comprising the steps of:
providing an indirect evaporative heat exchange section, the indirect heat exchange section conducting a fluid stream within a plurality of pathways, the indirect heat exchange section comprising a top and a bottom, moving air through the indirect section, the air moving through the indirect heat exchange section exchanging heat with the evaporative liquid moving through the indirect heat exchange section and hence indirectly exchanging heat with the fluid stream within the plurality of pathways in the indirect section, wherein the indirect heat exchange section is comprised of a series of serpentine coils comprising run sections and return bend sections, and certain of the return bend sections having a greater vertical spacing than other of the return bend sections, the inc

Assignees

• Baltimore Aircoil Co Inc

Inventors

• Aaron David Andrew
• Liu Zan
• Korenic Branislav
• Rule John Edward
• Blay Preston P
• Hollander Philip S

Classifications

• F28F25/06

  Spray nozzles or spray pipes · CPC title

• F28F25/12

  Ducts; Guide vanes, e.g. for carrying currents to distinct zones · CPC title

• F28F2250/08

  Fluid driving means, e.g. pumps, fans · CPC title

• F28D5/02

  in which the evaporating medium flows in a continuous film or trickles freely over the conduits · CPC title

• F28D7/082

  with serpentine or zig-zag configuration · CPC title