COOLING TOWER SPLASH FILL
A splash fill arrangement for use in a direct heat exchange section of a cooling tower is provided. Each splash fill arrangement includes support plates and elongated bars extending there between, which arrangement improves the performance of the splash fill arrangement when installed as a direct heat exchange section of a cooling tower. Certain of the elongated bars between the support plates are angled from the horizontal to improve the air flow capabilities and performance of the direct heat exchange section.
The present invention relates to a heat and mass transfer media, or a splash fill arrangement, utilized within the direct heat exchange portion of a cooling tower. More particularly, the present invention relates to a splash fill arrangement for use in a direct heat exchange unit, which could be a cooling tower.
The heat and mass transfer media, or splash fill arrangement, is generally horizontally oriented with an evaporative liquid, usually water, coursing over the arrangement, usually flowing downwardly, with an air stream directed usually transversely but potentially concurrent or cross current through the splash fill arrangement comprising a direct cooling section. The air interacts with the evaporative liquid for heat and mass transfer.
SUMMARY OF THE INVENTIONThe heat and mass transfer media, or splash fill arrangement, of the present invention enhances the thermal efficiency of the direct heat exchanger by providing an arrangement of splash fill components over which air and an evaporative liquid, usually water, pass. The arrangement of splash fill components is comprised of two or more support plates, between which a plurality of elongated bars extend. The elongated bars are positioned at predetermined locations and angles to provide an improved direct heat exchanger. The improved performance of the direct heat exchanger is related to the shape, positioning and angle placement of the elongated bars. By placing the elongated bars of the various preferred shapes at such preferred locations and angles, improved flow of the evaporative liquid, usually water, over the elongated bars occurs. Improved flow of the evaporative liquid includes improved drop formation and flow direction when the evaporative liquid drops leave the elongated bars. Such improved drop formation is combined with improved air flow between and across the elongated bars. This combination of improved drop formation and improved air flow leads to improved heat transfer in the direct heat exchanger.
When the evaporative liquid passes generally downwardly over the elongated bars of the splash fill arrangement, portions of the evaporative liquid spills from certain of the elongated bars, wraps around certain of the elongated bars and then falls from the bars or both. The cooling air which is usually drawn across the elongated bars by a fan causes some of the evaporative liquid to evaporate and thusly result in mass and heat transfer.
The cross sectional shape of the splash fill component elongated bar can be of various types, but usually includes rounded corners to allow the evaporative liquid to both flow across portions of and in some embodiments wrap around the cross section of the elongated bar. Such flow improves the heat transfer from the evaporative liquid and the air passing through the splash fill arrangement.
The splash fill elongated bars are usually angled downwardly from 5 to 45 degrees from the horizontal toward the air inlet side of the splash fill arrangement. This angled orientation of the elongated bars assists in exposing more of the evaporative liquid flowing across the bars to the air moving across the splash fill arrangement, without unduly impeding the air flow. In certain embodiments of the splash fill arrangement of the present invention, most arrays of elongated bars will be angled downwardly from 5 to 45 degrees from the horizontal, while an intermittent array of elongated bars will not be so angled, but rather be at a horizontal orientation.
In the drawings,
Referring now to
Referring now to
Referring now to
Air flow is depicted as from left to right in
The vertical gap 43 between elongated bars 44 and 46 varies such that the size of gap 43 near top edge 47 of support plate 40 is smallest and gradually increases toward the bottom edge 48. The gradual increase in the vertical gap 43 between elongated bars 44 and 46 helps to counteract the difference in air pull pressure along the outlet side 59 by the fan 12 that is generally located near the corner of top edge 47 and outlet side 59.
Referring now to
Referring now to
Claims
1. A splash fill arrangement for use in a direct heat exchanger, comprising
- a support plate and a plurality of elongated bars,
- the support plate including a plurality of openings, each support plate opening adapted to receive an elongated bar,
- at least one of the elongated bars set at an angle from the horizontal of between 5 and degrees.
2. The splash fill arrangement of claim 1 wherein
- at least one of the elongated bars has a generally smooth edged rectangular cross section.
3. The splash fill arrangement of claim 1 wherein
- at least one of the elongated bars has a generally smooth edged rectangular cross section with at least one raised ridge along a lower surface of the elongated bar.
4. The splash fill arrangement of claim 1 wherein at least one of the elongated bars has a generally smooth edged rectangular cross section with a top surface thereof generally raised from the horizontal and a bottom surface thereof indented from the horizontal.
5. The splash fill arrangement of claim 1 further comprising
- a second plurality of elongated bars located beneath the plurality of elongated bars and wherein at least one of the second plurality of elongated bars is set an angle of about 0 degrees from the horizontal.
6. The splash fill arrangement of claim 1 further comprising
- a second plurality of elongated bars, the second plurality of elongated bars positioned adjacent an air inlet of the direct heat exchanger and wherein at least one of the second plurality of elongated bars is set at an upward angle from the horizontal of between 5 and 45 degrees, and
- a third plurality of elongated bars, the third plurality of elongated bars positioned adjacent an air outlet of the direct heat exchanger and wherein at least one of the third plurality of elongated bars is set at a downward angle from the horizontal of between and 50 degrees.
7. The splash fill arrangement of claim 1 further comprising
- vertical gaps between elongated bars wherein the gaps are generally smallest near the top of support plate and gradually increase toward the bottom of plate.
8. A splash fill arrangement for use in a direct heat exchanger, comprising
- a support plate and a first plurality of elongated bars,
- the support plate including a plurality of openings, each support plate opening adapted to receive an elongated bar from the first plurality of elongated bars,
- a second plurality of elongated bars, each support plate opening adapted to receive an elongated bar from the second plurality of elongated bars.
- at least one of the first plurality of elongated bars set at an angle from the horizontal of between 5 and 45 degrees,
- at least one of the second plurality of elongated bars set at an angle of about 0 degrees from the horizontal, and wherein the second plurality of elongated bars is located generally between the first plurality of elongated bars.
9. The splash fill arrangement of claim 7 wherein
- at least one of the first plurality of elongated bars has a generally smooth edged rectangular cross section.
10. The splash fill arrangement of claim 7 wherein
- at least one of the first plurality of elongated bars has a generally smooth edged rectangular cross section with at least one raised ridge along a lower surface of the elongated bar.
10. The splash fill arrangement of claim 7 wherein at least one of the first plurality of elongated bars has a generally smooth edged rectangular cross section with a top surface thereof generally raised from the horizontal and a bottom surface thereof indented from the horizontal.
11. A splash fill arrangement for use in a direct heat exchanger, comprising
- a support plate and a first plurality of elongated bars,
- the support plate including a plurality of openings, each support plate opening adapted to receive an elongated bar from the first plurality of elongated bars,
- a second plurality of elongated bars, the second plurality of elongated bars positioned adjacent an air inlet of the direct heat exchanger and wherein at least one of the second plurality of elongated bars is set at an upward angle from the horizontal of between 5 and 45 degrees, and
- a third plurality of elongated bars, the third plurality of elongated bars positioned adjacent an air outlet of the direct heat exchanger and wherein at least one of the third plurality of elongated bars is set at a downward angle from the horizontal of between and 50 degrees.
12. The splash fill arrangement of claim 11 wherein
- at least one of the first plurality of elongated bars has a generally smooth edged rectangular cross section.
13. The splash fill arrangement of claim 11 wherein
- at least one of the first plurality of elongated bars has a generally smooth edged rectangular cross section with at least one raised ridge along a lower surface of the elongated bar.
14. The splash fill arrangement of claim 11 wherein at least one of the first plurality of elongated bars has a generally smooth edged rectangular cross section with a top surface thereof generally raised from the horizontal and a bottom surface thereof indented from the horizontal.
15. The splash fill arrangement of claim 11 further comprising
- vertical gaps between elongated bars wherein the gaps are generally smallest near the top of support plate and gradually increase toward the bottom of plate.
16. The splash fill arrangement of claim 11 wherein
- at least one of the first plurality of elongated bars has an opening
- in a lower surface of the elongated bar.
Type: Application
Filed: Oct 22, 2015
Publication Date: Apr 27, 2017
Inventors: Yoon Shin (Ellicott City, MD), Andrew Sickler (Bradenton, FL), Kevin Deliman (Pittsburgh, PA), Trevor Fontes (Jessup, MD), David Andrew Aaron (Reisterstown, MD)
Application Number: 14/919,960