Indirect heat exchanger having circuit tubes with varying dimensions

Patent metadata

Field	Value
Publication number	US-10655918-B2
Application number	US-201615291773-A
Country	US
Kind code	B2
Filing date	Oct 12, 2016
Priority date	Oct 12, 2016
Publication date	May 19, 2020
Grant date	May 19, 2020

Abstract

An improved indirect heat exchanger is provided which is comprised of a plurality of coil circuits, with each coil circuit comprised of an indirect heat exchange section tube run or plate. Each tube run or plate has at least one change in its geometric shape or may have a progressive change in its geometric shape proceeding from the inlet to the outlet of the circuit. The change in geometric shape along the circuit length allows simultaneously balancing of the external airflow, internal heat transfer coefficients, internal fluid side pressure drop, cross sectional area and heat transfer surface area to optimize heat transfer.

First claim

What is claimed is:

1. An indirect heat exchanger comprising:
a plurality of coil circuits,
an inlet header connected to an inlet end of each coil circuit and an outlet header connected to an outlet end of each coil circuit,
an evaporative fluid supply configured to distribute evaporative fluid downward onto the coil circuits;
a sump configured to collect evaporative fluid that falls off the coil circuits;
a pump configured to pump evaporative fluid from the sump to the evaporative fluid supply;
a fan;
a motor connected to the fan and operable to cause air to move over the coil circuits;
each coil circuit including a circuit tube that extends in a series of run lengths and return bends from the inlet end of each coil circuit to the outlet end of each coil circuit,
each circuit tube having a decreasing horizontal cross sectional dimension and an increasing vertical cross sectional dimension as the circuit tube extends from adjacent the inlet end of each coil circuit to adjacent the outlet end of each coil circuit,
the plurality of coil circuits including a first coil circuit having first, second, third, fourth, and fifth circuit tube run lengths,
the first circuit tube run length of the first coil circuit having a circular cross section and extending from the inlet header to one of the return bends of the first coil circuit,
the first circuit tube run length having a cylindrical outer surface extending from the inlet header to the one return bend,
the second and third circuit tube run lengths both having the same cross-sectional shape including a first horizontal cross sectional dimension and a first vertical cross sectional dimension; and
the fourth and fifth circuit tube run lengths both having the same cross-sectional shape including a second horizontal cross sectional dimension less than the first horizontal cross sectional dimension and a second vertical cross sectional dimension larger than the first vertical cross sectional dimension.

2. The indirect heat exchanger of claim 1
wherein a first ratio of the vertical cross sectional dimension of each circuit tube run length to the horizontal cross sectional dimension of each circuit tube run length exists adjacent the inlet end of each coil circuit, and a second ratio of the vertical cross sectional dimension of each circuit tube run length to the horizontal cross sectional dimension of each circuit tube run length exists adjacent the outlet end of each coil circuit, and wherein the second ratio is larger than the first ratio.

3. The indirect heat exchanger of claim 2
wherein the first ratio is between 1.0 and 2.0, and the second ratio is greater than the first ratio but less than 6.0.

4. The indirect heat exchanger of claim 1
wherein each circuit tube is comprised of galvanized steel, stainless steel, aluminum, or copper.

5. The indirect heat exchanger of claim 1
wherein each individual circuit tube run length is of a uniform horizontal cross sectional dimension and a uniform vertical cross sectional dimension between return bends, and wherein the horizontal cross sectional dimension of the circuit tube run lengths decrease adjacent to the outlet end of each coil circuit and the vertical cross sectional dimension of the circuit tube run lengths increase adjacent to the outlet end of each coil circuit.

6. The indirect heat exchanger of claim 1
wherein each circuit tube return bend is circular in cross section.

7. The indirect heat exchanger of claim 1
wherein each circuit tube run length at the inlet end of each coil circuit as connected to the inlet header is circular in cross section.

8. An indirect heat exchanger comprising:
a plurality of coil circuits,
an inlet header connected to an inlet end of each coil circuit and an outlet header connected to an outlet end of each coil circuit,
an evaporative fluid supply configured to distribute evaporative fluid downward onto the coil circuits;
a sump configured to collect evaporative fluid that falls off the coil circuits;
a pump configured to pump evaporative fluid from the sump to the evaporative fluid supply;
a fan;
a motor connected to the fan and operable to cause air to move over the coil circuits;
each coil circuit including a circuit tube that extends in a series of run lengths and return bends from the inlet end of each coil circuit to the outlet end of each coil circuit,
each circuit tube run length having a single pre-selected horizontal cross sectional dimension and a single pre-selected vertical cross sectional dimension for the entire length of the circuit tube run length,
with the horizontal cross sectional dimension of the individual run lengths decreasing and the vertical cross sectional dimension of the individual run lengths increasing as the circuit tubes extend from adjacent the inlet end of each coil circuit to adjacent the outlet end of each coil circuit,
at least one of the circuit tubes having a vertical distance between adjacent run lengths of the respective circuit tube with the vertical distance decreasing as the respective circuit tube extends from adjacent the inlet header to adjacent the outlet header;
a first horizontal distance between adjacent run lengths of a first and second circuit tube, directly connected to the inlet header; and
a second horizontal distance between adjacent run lengths of the first and second circuit tube, directly connected to the outlet header; wherein
the first distance is smaller than the second distance;
wherein the run lengths of each circuit tube have a uniform circumference;
the run lengths of one of the coil circuits including a first run length,
the return bends of the one coil circuit including a first pair of return bends, and
the first run length having a cylindrical outer surface extending from one of the first pair of return bends to the other of the first pair of return bends.

9. The indirect heat exchanger of claim 8
wherein a first ratio of a vertical cross sectional dimension of each circuit tube run length to the horizontal cross sectional dimension of each circuit tube run length exists adjacent the inlet end of each coil circuit, and a second ratio of the vertical cross sectional dimension of each circuit tube run length to the horizontal cross sectional dimension of each circuit tube run length exists adjacent the outlet end of each coil circuit, and wherein the second ratio is larger than the first ratio.

10. The indirect heat exchanger of claim 9
wherein the first ratio is between 1.0 and 2.0, and the second ratio is greater than the first ratio but less than 6.0.

11. The indirect heat exchanger of claim 8
wherein each circuit tube is comprised of galvanized steel, stainless steel, aluminum, or copper.

12. The indirect heat exchanger of claim 8 wherein each individual circuit tube run length is of a uniform horizontal cross sectional dimension and a uniform vertical cross sectional dimension between return bends, and wherein the horizontal cross sectional dimension of each run length decreases adjacent to the outlet end of each circuit tube and the vertical cross sectional dimension of each run length increases adjacent to the outlet end of each coil circuit.

13. The indirect heat exchanger of claim 8
wherein each circuit tube return bend is circular in cross section.

14. An indirect heat exchanger comprising:
a plurality of coil circuits,
an inlet header connected to an inlet end of each coil circuit and an outlet header connected to an outlet end of each coil circuit,
an evaporative fluid supply configured to distribute evaporative fluid downward onto the coil circuits;
a sump

Assignees

• Baltimore Aircoil Co Inc

Inventors

• Beaver Andrew
• Aaron David Andrew
• Rousselet Yohann Lilian

Classifications

• F28D1/0477 Primary

  the conduits being bent in a serpentine or zig-zag · CPC title

• F28C3/06 Primary

  the heat-exchange media being a liquid and a gas or vapour (temperators for cooling steam F22) · CPC title

• F28F21/084

  from aluminium or aluminium alloys · CPC title

• F28D1/047

  the conduits being bent, e.g. in a serpentine or zig-zag · CPC title

• F28F1/025

  with variable shape, e.g. with modified tube ends, with different geometrical features (F28F1/06, F28F1/08, F28F9/16, F28F9/18 take precedence) · CPC title