Intertwined helical heat exchanger

• US 6,044,837 A
• Filed: 05/12/1998
• Issued: 04/04/2000
• Est. Priority Date: 05/12/1998
• Status: Expired due to Term

• Current Assignee: Harry Arthur Tyler
• Original Assignee: Harry Arthur Tyler
• Inventors: Tyler, Harry Arthur
• Primary Examiner(s): Lazarus, Ira S.
• Assistant Examiner(s): Cocks, Josiah C.
• Application Number:
  US09/076,685
• Time in Patent Office: 693 Days
• Field of Search: 126/99 C, 126/99 R, 126/99 A, 126/99 D, 126/109, 126/110 R, 126/116 R, 126/6, 126/67, 126/72, 432/223, 122/367.1, 122/367.2, 122/367.3, 122/250 R, 122/249, 122/DIG. 1, 122/DIG. 2, 122/356, 122/13.1, 122/14, 165/163
• US Class Current: 126/99.00C
• CPC Class Codes: F24H 3/065 using fluid fuel
• CPC Class Codes: Y10S 122/02 Air heater - indirectly heated

Abstract

A combustion and heating chamber into which a fluid is pumped under pressure is provided. A burner is positioned in the combustion and heating chamber to provide a heat load to the pressurized fluid in the chamber. As the fluid is heated its internal pressure is greatly raised providing a force for driving the heated air through a spiral conduit that encircles the combustion and heating chamber. An insulated outer wall is fitted around the spiral conduit and in contact with it. The individual wraps of the spiral conduit do not lay side by side, but are spaced apart. Relatively cool process air is drawn into the spaces between the separate wraps of the spiral conduit, which is thereby formed as a second spiral space intertwined with the spiral conduit between the combustion and heating chamber wall and the outer wall. The process fluid is therefore in contact with the walls of the spiral conduit. Preferably, as the heated fluid spirals in a downward direction under pressure and cooling as it moves downwardly, its heat is transferred through the walls of the spiral conduit into the space between the individual coils of the spiral conduit so as to heat the relatively cooler process air which is spiraling upwardly at the same time and being heated as it moves.

Claims

1. A heat exchanger apparatus comprising:

an outer cylindrical chamber wall enclosing a coaxially positioned inner cylindrical chamber wall defining a combustion and heating chamber, the outer and inner cylindrical chamber walls defining an annular space therebetween;

a burner positioned for throwing a flame axially within the combustion and heating chamber for raising the temperature of a heating fluid therewithin;

a tubular conduit wound as a spiral about the inner cylindrical chamber wall, the tubular conduit being of such diameter as to partition the annular space between the inner and the outer cylindrical chamber walls to form a continuous helical space therein;

the tubular conduit providing a conduit inlet aperture joining the tubular conduit with the inner chamber adjacent the burner, for drawing the heating fluid from the combustion and heating chamber into the tubular conduit, and firther providing a conduit outlet aperture positioned at the outer cylindrical wall distally from the burner for expending the heating fluid from the tubular conduit;

a process fluid inlet positioned distally from the burner for drawing a process fluid into the helical space between the inner and outer cylindrical walls; and

a process fluid outlet positioned adjacent to the burner for expending the process fluid from the helical space.

2. The apparatus of claim 1 wherein the burner is oriented for directing the flame downwardly.

3. The apparatus of claim 1 wherein the outer cylindrical chamber wall provides a means for thermal insulation.

4. The apparatus of claim 3 further comprising a base for supporting the apparatus thereupon.

5. The apparatus of claim 1 wherein the inner and outer cylindrical walls are circular in cross-section.

6. The apparatus of claim 1 wherein the tubular conduit is constructed with a corrugated wall capable of conforming to the inner cylindrical chamber wall.

7. The apparatus of claim 6 wherein the corrugated wall is of such shape as to provide a surface area of at least four times that of a corresponding straight wall tubular conduit.