Thermal capacity of elliptically finned heat exchanger

• US 10,288,352 B2
• Filed: 01/09/2017
• Issued: 05/14/2019
• Est. Priority Date: 01/08/2016
• Status: Active Grant

• Current Assignee: Evapco Incorporated
• Original Assignee: Evapco Incorporated
• Inventors: Bugler, Thomas W.
• Primary Examiner(s): Ruby, Travis C
• Application Number:
  US15/402,069
• Publication Number:
  US 20170198973A1
• Time in Patent Office: 855 Days
• CPC Class Codes: F28B 1/06 using air or other gas as the cooling medium
• CPC Class Codes: F28C 1/14 comprising also a non-direct contact heat exchange
• CPC Class Codes: F28D 1/0477 the conduits being bent in a serpentine or zig-zag
• CPC Class Codes: F28D 5/02 in which the evaporating medium flows in a continuous film or trickles freely over the conduits
• CPC Class Codes: F28F 1/02 Tubular elements of cross-section which is non-circular F28F1/08, F28F1/10 take precedence
• CPC Class Codes: F28F 1/36 the means being helically wound fins or wire spirals

Abstract

Spiral finned elliptical tube closed circuit coolers and evaporative refrigerant condensers in which the air flow entering the unit is directed to flow across the tubes in a direction that is parallel to the tube axes and generally perpendicular to the fins produce a completely unexpected gain in capacity of 25% compared to comparable units in which the air flow is directed across/perpendicular to the tube axes.

Claims

1. An evaporative heat exchanger for cooling or condensing a process fluid, consisting essentially of:

an indirect evaporative heat exchange section;

a direct heat exchange section situated beneath the indirect evaporative heat exchange section;

a water distribution system located above the indirect evaporative heat exchange section and configured to spray water over the indirect evaporative heat exchange section;

the indirect evaporative heat exchange section comprising a process fluid inlet header and a process fluid outlet header, and an array of serpentine tubes connecting said inlet header and said outlet header, said serpentine tubes having an elliptical cross-section with spiral fins;

said serpentine tubes further having lengths extending along a longitudinal axis, said lengths connected to adjacent lengths of a same serpentine tube by tube bends;

said direct section comprising a plenum where water distributed by said water distribution system and having received heat from said indirect evaporative heat exchange section is cooled by direct contact with air moving through said plenum;

a water recirculation system, including pump and pipes, configured to take water collecting in a basin at the bottom of said plenum and deliver it to said water distribution system;

an air mover configured to move ambient air into said plenum and up through said indirect evaporative heat exchange section;

wherein said evaporative heat exchanger is configured so that air is moved by said air mover into said plenum in a direction that is parallel to said longitudinal axis of said tube lengths and perpendicular to longitudinal axes of said spiral fins.

2. The evaporative heat exchanger according to claim 1, wherein substantially all air flow driven by said air mover into said indirect evaporative heat exchange section flows first through said plenum.

3. The evaporative heat exchanger according to claim 1, wherein said air mover is a fan, and said evaporative heat exchanger is an induced draft device and said fan is located above said water distribution system, and is configured to draw air from outside of said device into said plenum and up through said indirect evaporative heat exchange section.

4. The evaporative heat exchanger according to claim 3, wherein sides of said plenum parallel to said tube lengths are sealed to prevent substantial entry of air.

5. The evaporative heat exchanger according to claim 1, wherein is said air mover is a fan, and said evaporative heat exchanger is a forced draft device, and said fan is located at a side of said plenum that is beneath said tube bends.

6. The evaporative heat exchanger according to claim 5, wherein said longitudinal axis of said tube lengths is perpendicular to a longitudinal axis of said evaporative heat exchanger.

7. The evaporative heat exchanger according to claim 5, wherein said fan is configured to draw air from outside of said device and force it into said plenum in a direction that is parallel to said longitudinal axis of said tube lengths and perpendicular to longitudinal axes of said spiral fins.

8. The evaporative heat exchanger according to claim 7, wherein substantially all air flow entering said indirect evaporative heat exchange section is delivered by said fan.

9. The evaporative heat exchanger according to claim 8, wherein substantially no air enters said plenum except via said fan.

10. The evaporative heat exchanger according to claim 1, wherein said air mover is a first fan and a second fan, said first fan located at a side of said plenum that is beneath a set of tube bends at a first end of said tube lengths, said second fan located at a side of said plenum that is beneath a set of tube bends at a second end of said tube lengths.

11. The evaporative heat exchanger according to claim 10, wherein said fans are configured to draw air from outside of said device and force it into said plenum in a direction that is parallel to said longitudinal axis of said tube lengths and perpendicular to longitudinal axes of said spiral fins.