The present disclosure relates generally to condensate pans and condensate traps for furnace applications in HVAC&R systems.
The basic components of a furnace system include a burner; a heat exchanger; an air distribution system; and a vent pipe. In the burner, a fuel, often gas (natural or propane) or oil, is delivered and burned to generate heat. The heat exchanger is used to transfer the heat from the burning fuel to the air distribution system. The air distribution system, which generally includes a blower and ductwork, delivers the heated air to the space to be heated and returns cooler air to the furnace. The vent pipe or flue exhausts byproducts of combustion to the external environment.
In high efficiency furnaces, also commonly referred to as condensing furnaces, significant amounts of water condense from the flue gas within the heat exchanger that must be collected in a condensate pan and drained separately from the flue gas exiting by the vent pipe. Conventional condensate traps are external to the condensate pan and typically require an extra 6 to 8 inches of clearance that is not always readily available.
Furthermore, furnaces are generally manufactured so that each furnace can be installed vertically or horizontally in any one of four configurations—upflow, downflow, horizontal right or horizontal left. The furnaces are usually shipped from the factory with the condensate trap and associated drain hoses already installed for one of these configurations, so the furnace installer must ordinarily move the condensate trap to a new position if the furnace is to be installed in one of the three other configurations.
Intended advantages of the disclosed systems and/or methods satisfy one or more of these needs or provide other advantageous features. Other features and advantages will be made apparent from the present specification. The teachings disclosed extend to those embodiments that fall within the scope of the claims, regardless of whether they accomplish one or more of the aforementioned needs.
One embodiment relates to a condensate pan for use in a condensing furnace that has an internal condensate trap. The condensate trap may be formed integral with the condensate pan.
Another embodiment relates to a condensate pan that has multiple internal condensate traps for use in a multi-position condensing furnace so that the same condensate pan can be used in any one of the different furnace positions.
Certain advantages of the embodiments described herein are that by making the condensate trap internal to the condensate pan, external condensate traps may be eliminated resulting in desirable space savings, among other advantages which will be readily apparent to those of ordinary in skill upon reviewing the present disclosure. Furthermore, by making the condensate trap internal to the condensate pan, additional labor associated with moving the condensate trap to an alternate position can be avoided, for example, when the furnace is a multi-position furnace that is to be installed in a configuration different than shipped from the factory.
Alternative exemplary embodiments relate to other features and combinations of features as may be generally recited in the claims.
As combustion air 102 exchanges heat with supply air 104, a portion of the water vapor in combustion air 102 condenses to a liquid. A resultant liquid condensate 113 emerges from second heat exchanger 105 and falls into a condensate pan 120 and is eventually directed out of the condensing furnace 100. Likewise, the uncondensed portion of combustion air 102 emerges from second heat exchanger 105 as exhaust 111 and is removed from furnace 100 by use of an exhaust blower, or inducer, 109 or similar air-moving device through a vent, such as vent pipe 115. Exhaust 111 includes air, water vapor and other combustion products.
Condensate 113 formed in second heat exchanger 105, in addition to water, may contain combustion products and other contaminants that can be acidic and/or corrosive. Second heat exchanger 105 and the areas in which the liquid condensate 113 forms and flows can be fabricated using corrosion resistant materials such as stainless steel (e.g., 29-4c stainless steel) or other heat resistant, corrosion resistant materials, such as plastic.
Referring to
The cooled byproducts leave the heat exchanger section of furnace 100 at the outlet 106 of second heat exchanger 105 where exhaust 111 is eliminated via vent pipe 115, while liquid condensate 113 falls by gravity to the bottom of condensate pan 120.
Condensate pan 120 is positioned intermediate second heat exchanger outlet 106 and inducer 109 that draws combustion air 102 from the heat exchangers as exhaust 111 and forces it out of vent pipe 115. The condensate pan 120 is firmly mounted to vestibule 130 to reduce and/or prevent exhaust 111 or liquid condensate 113 from leaving condensing furnace 100 other than first passing through condensate pan 120.
Turning to
As illustrated in
Where multiple separate pieces are used for pan cover 122 and pan body 124, a heat seal or glue can be employed between them to prevent leaking A gasket 137 may be formed or embedded in either the pan cover 122 and/or pan body 124 to seal the outer surfaces against inducer 109 and/or vestibule 130. Alternatively, the gasket may be provided as a separate piece to be inserted during assembly. As also shown in
As the exhaust 111 entering condensate pan 120 from second heat exchanger 105 is removed by the inducer mounted to the exterior surface 129 (
The condensate trap 128 is bounded by the bottom wall 160 of the condensate pan 120 and a top cover. The top cover is generally provided by pan cover 122; however the top cover may be provided by vestibule 130, for example, if pan body 124 is mounted directly to vestibule 130. The condensate pan bottom wall 160 and top cover act as vertical side walls of condensate trap 128 when in use. As shown in
As liquid condensate 113 enters into main chamber 126, it flows into condensate channel 125 and enters trap 128 at a gate 168 at the end of condensate channel 125. The liquid condensate 113 begins to fill trap 128 from the bottom up and rises until it reaches main drain 140 that allows the liquid to flow out of condensate pan 120, usually through a drain hose 170 to the sewer or other external source. Baffle 127 is formed within condensate pan 120 at a pre-determined location, having a pre-determined length and spaced a pre-determined width away from side wall 162 such that under steady state conditions during condensing furnace operation, liquid condensate 113 flowing into trap 128 substantially matches the liquid condensate 113 flowing out of condensate trap 128. Baffle 127 is further formed and positioned so that there is a steady state liquid level within trap 128 both high enough to maintain a barrier of liquid between inducer 109 and main drain 140 and low enough that the liquid does not substantially back up into main chamber 126 under ordinary conditions. More particularly, the baffle 127 can be positioned so that the gate 168 and channel 125 are sufficiently narrow that condensate 113 backs up into channel 125 to a level higher than in trap 128 under steady state operating conditions.
Those of ordinary skill in the art will readily appreciate that determining the appropriate dimensions and positioning of baffle 127 depends on the strength of the particular inducer 109 to be used in conjunction with condensate pan 120. The more powerful the inducer 109, the stronger the draw on the condensate 113, and the longer or wider the channel 125 and/or the wider the gate 168 needed to provide a reservoir of condensate 113 between main chamber 126 and main drain 140.
Keeping liquid between main chamber 126 and main drain 140 avoids sewer gas being drawn by inducer 109 from main drain 140 back into condensate pan 120. Keeping liquid from backing up into main chamber 126 reduces the likelihood of system malfunction, which can occur due to a rise in pressure if water backs up into second heat exchanger 105. The main chamber 126 can also include one or more blocked condensate tabs 144, which can be connected to a pressure switch, so that if the liquid level rises faster than it can drain, the furnace 100 can be shut down.
In addition to main drain 140, condensate trap 128 can also include a flue drain 142. The flue drain 142 allows a flue drain hose 172 or other connection to vent pipe 115 so that any liquid condensate 113 that might form in vent pipe 115 as exhaust 111 continues to cool, flows back to condensate pan 120 and can be drained. Thus, while condensate 113 flows out of pan 120 via main drain 140, condensate 113 forming in vent pipe 115 flows back into pan 120 via flue drain 142. Flue drain 142 can be positioned below its associated main drain 140 so that any condensate 113 from vent pipe 115 enters condensate trap 128 below the steady state liquid level, preventing inducer 109 from drawing discharged exhaust 111 back into condensate pan 120. This can further be achieved by positioning flue drain 142 near the gate 168 within condensate channel 125.
As illustrated in
Turning to
While each trap 128 generally has its own main drain 140 and flue drain 142, condensate pan 120 may include as few as two blocked condensate tabs 144. Alternatively, a separate blocked condensate tab 144 can be provided for each condensate trap 128 or any intermediate number may also be provided, as illustrated in
The geometry of condensate pan 120, as well as the number and placement of condensate traps 128, main drains 140, flue drains 142, blocked condensate tabs 144 and inducer aperture 135 can all be adjusted as desired, as illustrated for example, by the different shaped pan bodies 124 shown in
It should be understood that the application is not limited to the details or methodology set forth in the following description or illustrated in the figures. It should also be understood that the phraseology and terminology employed herein is for the purpose of description only and should not be regarded as limiting.
While the exemplary embodiments illustrated in the figures and described herein are presently preferred, it should be understood that these embodiments are offered by way of example only. Accordingly, the present application is not limited to a particular embodiment, but extends to various modifications that nevertheless fall within the scope of the appended claims. The order or sequence of any processes or method steps may be varied or re-sequenced according to alternative embodiments.
It is important to note that the construction and arrangement of the condensate pan as shown in the various exemplary embodiments is illustrative only. Although only a few embodiments have been described in detail in this disclosure, those skilled in the art who review this disclosure will readily appreciate that many modifications are possible (e.g., variations in sizes, dimensions, structures, shapes and proportions of the various elements, values of parameters, mounting arrangements, use of materials, colors, orientations, etc.) without materially departing from the novel teachings and advantages of the subject matter recited in the claims. For example, elements shown as integrally formed may be constructed of multiple parts or elements, the position of elements may be reversed or otherwise varied, and the nature or number of discrete elements or positions may be altered or varied. Accordingly, all such modifications are intended to be included within the scope of the present application. Other substitutions, modifications, changes and omissions may be made in the design, operating conditions and arrangement of the exemplary embodiments without departing from the scope of the present application.
This application is a continuation of U.S. application Ser. No. 11/856,889, filed Sep. 18, 2007, which claims the benefit of U.S. Provisional Application No. 60/945,978, filed Jun. 25, 2007, which Applications are hereby incorporated by reference.
Number | Name | Date | Kind |
---|---|---|---|
1029696 | Kopper | Jun 1912 | A |
1058781 | Mouat | Apr 1913 | A |
1065690 | Kopper | Jun 1913 | A |
1839516 | Wetherbee | Jan 1932 | A |
1976879 | Ewer | Oct 1934 | A |
2013237 | Funk | Sep 1935 | A |
2013685 | Reed-Hill | Sep 1935 | A |
4289730 | Tomlinson | Sep 1981 | A |
4603680 | Dempsey et al. | Aug 1986 | A |
4835984 | Vyavaharkar et al. | Jun 1989 | A |
4903723 | Sublett | Feb 1990 | A |
4938203 | Thrasher et al. | Jul 1990 | A |
4939833 | Thomas | Jul 1990 | A |
5099873 | Sanchez | Mar 1992 | A |
5199457 | Miller | Apr 1993 | A |
5309890 | Rieke et al. | May 1994 | A |
5313930 | Kujawa et al. | May 1994 | A |
5320087 | Froman | Jun 1994 | A |
5375586 | Schumacher et al. | Dec 1994 | A |
5379749 | Rieke et al. | Jan 1995 | A |
5379751 | Larsen et al. | Jan 1995 | A |
5408986 | Bigham | Apr 1995 | A |
5429274 | Vlaskamp | Jul 1995 | A |
5437303 | Johnson | Aug 1995 | A |
5439050 | Waterman et al. | Aug 1995 | A |
5448986 | Christopher et al. | Sep 1995 | A |
5582159 | Harvey et al. | Dec 1996 | A |
5704343 | Ahn et al. | Jan 1998 | A |
5749355 | Roan et al. | May 1998 | A |
5775318 | Haydock et al. | Jul 1998 | A |
6041959 | Domanico | Mar 2000 | A |
6116266 | Dickison et al. | Sep 2000 | A |
6283144 | Kahn | Sep 2001 | B1 |
6639517 | Chapman et al. | Oct 2003 | B1 |
6923173 | Schonberger, Sr. | Aug 2005 | B2 |
6938639 | Robinson | Sep 2005 | B1 |
6976367 | Spanger | Dec 2005 | B2 |
7036498 | Riepenhoff et al. | May 2006 | B2 |
7489253 | Murphy | Feb 2009 | B2 |
7637387 | Cantolino | Dec 2009 | B1 |
20050138939 | Spanger | Jun 2005 | A1 |
20050155535 | Rieke et al. | Jul 2005 | A1 |
20070151604 | Platusich et al. | Jul 2007 | A1 |
20100095687 | Tuszkiewicz et al. | Apr 2010 | A2 |
20110174289 | Paller et al. | Jul 2011 | A1 |
Number | Date | Country |
---|---|---|
2125092 | Jul 1997 | CA |
Number | Date | Country | |
---|---|---|---|
20120055465 A1 | Mar 2012 | US |
Number | Date | Country | |
---|---|---|---|
60945978 | Jun 2007 | US |
Number | Date | Country | |
---|---|---|---|
Parent | 11856889 | Sep 2007 | US |
Child | 13295556 | US |