Cooling tower with indirect heat exchanger
View Patent ↗A heat exchange apparatus is provided with an indirect evaporative heat exchange section. The indirect evaporative heat exchange section includes 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 including a series of serpentine tubes with run sections and return bend sections of both normal and increased height. A direct heat exchange section may be provided in the vertical spacing between run sections formed by the increased height return bends.
1. 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 heat exchange 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 normal and increased height 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 increased height return bend sections which have a height greater than the normal return bend sections,
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.
2. The method of exchanging heat of claim 1
wherein a distribution system is provided to distribute an evaporative liquid onto a portion of the indirect heat exchange section from a position below the top of the indirect heat exchange section in the area of the indirect heat exchange section having increased vertical spacing between vertically adjacent run sections of the series of serpentine tubes.
3. The method of exchanging heat of claim 1 wherein
a direct heat exchange section is provided beneath the distribution system, such direct heat exchange section comprising 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.
4. The method of exchanging heat of claim 1 wherein
the air moves generally upward through the indirect heat exchange section.
5. The method of exchanging heat of claim 1 wherein the air moves generally across the indirect heat exchange section.
6. The method of exchanging heat of claim 1 wherein the increased height of the return bend sections is at least one inch.
7. The method of exchanging heat of claim 2 , further comprising:
a drift eliminator located above the distribution system that distributes liquid over the indirect heat exchange section.
8. 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,
distributing an evaporative liquid onto 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 heat exchange section,
the air moving through the indirect heat exchange section exchanging heat and mass 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 normal height return bend sections and at least one increased height return bend section,
the increased height return bend section providing increased vertical spacing between vertically adjacent run sections of the serpentine coils,
an inlet header and
an outlet header operatively connected to the series of serpentine coils such that the fluid stream can pass into and
out from the series of serpentine tubes.
9. The method of exchanging heat of claim 8 ,
wherein the air moves generally upward through the indirect heat exchange section.
10. The method of exchanging heat of claim 8 ,
wherein a direct heat exchange section is provided 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.
11. The method of exchanging heat of claim 8 wherein
a distribution system is provided to distribute an evaporative liquid through the indirect heat exchange section from a position above the indirect heat exchange section.
12. The method of exchanging heat of claim 8 wherein
the air moves generally across the indirect heat exchange section.
13. The method of exchanging heat of claim 8
wherein the increased height of the return bend sections is at least one inch.
14. 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,
distributing an evaporative liquid onto 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 heat exchange 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 normal and increased height 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 increased height return bend sections which have a height greater that the normal return bend sections.
15. The method of exchanging heat of claim 14 , 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 it can be distributed onto the indirect heat exchange section.
16. The method of exchanging heat of claim 14
wherein a direct heat exchange section is provided 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.
17. The method of exchanging heat of claim 14 wherein
a distribution system is provided to distribute the evaporative liquid onto the indirect heat exchange section from a position above the indirect heat exchange section.
18. The method of exchanging heat of claim 14 wherein
a direct heat exchange section is provided, such direct heat exchange section comprising 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.
19. The method of exchanging heat of claim 14 , wherein
a direct heat exchange section is provided, such direct heat exchange section comprising a fill assembly located beneath the indirect heat exchange section, and moving air across the direct heat exchange section.
20. The method of exchanging heat of claim 14 , wherein
a drift eliminator is provided above the distribution system that distributes liquid over the indirect heat exchange section.