The present invention relates to a downdraft boiler and, more particularly, a downdraft boiler with tubulators.
Normally the burner in a boiler is provided below the heat exchanger so that the flow of flue gases is upwardly through the heat exchanger to the flue of the boiler.
Downdraft boilers are, of course, also known in which the burner may be at the top of the boilers and the flue gases are conducted downwardly through the heat exchanger and then pass from the heat exchanger chamber to the flue of the boiler.
An important advantage of a downdraft boiler is that it can be significantly more compact than a boiler in which the flue gases flow upwardly through the heat exchanger.
However, a major problem with downdraft boilers, especially in a compact configuration, is that the burner may be directly juxtaposed with the uppermost tubes of the heat exchanger, thereby causing overheating of the water in those tubes, inappropriate boiling so that gas formation may impede the flow of water through the tubes, and encrustation of these tubes with deposits from the water which passes through the tubes.
It is, therefore, the principal object of the present invention to provide an improved downdraft boiler whereby the aforementioned drawbacks are avoided.
More specifically, it is an object of this invention to provide a downdraft boiler in which overheating of at least the uppermost heat exchanger tubes can be avoided. A corollary object of the invention is to prevent, in a downdraft boiler, the undesired vaporization of water.
A further object of this invention is to provide an improved heat exchanger assembly, e.g. for use in a hot water generating unit.
These objects and others which will become apparent hereinafter are attained, in accordance with the invention, in a downdraft boiler for producing heated water for space heating purposes primarily and which comprises:
The burner can be a horizontal flat ceramic burner juxtaposed with the heat exchanger, the heat exchanger having an upper layer of the tubes, each provided with a respective such twisted baffle.
The tubes can be so-called finned tubes, i.e. tubes which are provided with heat exchanger fins or tubes which are formed by closely spaced fins having formations interfitting with one another. In any event the heat exchanger itself is provided with closely spaced vertical fins connected to the tubes.
Each of the fins can be traversed by a number of tubes and there can be an upper array of such fins which have a greater separation above the lower array of fins, the upper array being for example traversed by two horizontal rows of tubes while the lower array is traversed by only one row of tubes.
The heat exchanger assembly itself, for use in such a boiler or independently, i.e. for other heat exchanger purposes, can form a unit consisting of the fins and tubes and a pair of plates at opposite ends through which the tubes emerge and where the tubes can be interconnected by elbows and/or tees to permit water flow from an inlet fitting to an outlet fitting.
While it has been found to be advantageous to have a twisted baffle in each of the uppermost tubes of the heat exchanger or the row of tubes closest to the heating source, it has also been discovered that the twisted baffles greatly improve the overall effectiveness of the heat exchanger and thus that each such tube of the heat exchanger should be provided with a respective twisted baffle. The twisted baffle can be sheet metal strips having a helical twist whereby edges of said strips lie along respective helices.
Internal baffles within a heat exchanger tube are of course known and reference may be made to the turbulator of U.S. Pat. No. 4,044,796.
The above and other objects, features, and advantages will become more readily apparent from the following description, reference being made to the accompanying drawing in which:
From
Within the housing (
Below the combustion chamber 15, the boiler is formed with a heat exchanger chamber 21 receiving a heat exchanger assembly 22 which is traversed by water.
The heat exchanger assembly itself comprises an array of upper fins 23 traversed by a row of upper tubes 24 and less closely spaced than the lower fins 25 of another fin array. In the embodiment illustrated (see especially
As will be apparent from
The terminal plate at the opposite end of the heat exchange assembly has been represented at 35.
As can be seen at 36 in
The twisted baffle or turbulator 36 (see
In
In operation, while the water to be heated is circulated through the heat exchanger assembly, the flue gases produced by the ceramic burner pass downwardly between the fins, heating the water in the tubes. Undesired vaporization of the water is prevented by the turbulators of at least the upper row of tubes.
Number | Name | Date | Kind |
---|---|---|---|
4044796 | Smick | Aug 1977 | A |
4095087 | Giraud | Jun 1978 | A |
4738225 | Juang | Apr 1988 | A |
5566648 | Fenn et al. | Oct 1996 | A |
5799622 | Waldner | Sep 1998 | A |
6810836 | Ferguson et al. | Nov 2004 | B1 |