1. Field of the Invention
The present invention generally relates to a furnace, and more particularly to a furnace comprising a burner for burning a renewable fuel source.
2. Background Art
The advantages of using renewable fuel sources to produce thermal energy are well known. Cereal and corn kernels as well as wood pellets are among the readily renewable fuel sources that are presently being explored for thermal energy production. For example, corn is readily available naturally as kernels and provides competitive pricing per unit of energy produced. However, the use of corn as a fuel source has presented several challenges One such challenge is the delivery of the kernels to the combustion chamber of the burner in a heating system such as a furnace. Another challenge is the requirement for proper temperature, mixing and oxygen exposure. A further challenge is maintaining optimum temperature control of the burner and of the furnace as a whole.
Therefore, there exists a need for improvements in the art of burning renewable fuel sources.
Therefore, in accordance with an aspect of the present invention, there is provided a furnace comprising a housing defining a combustion chamber therein, a burner in the housing, the burner comprising a body defining a burning zone, a fuel feeder in communication with the burning zone adapted to feed a renewable fuel source therein, an air supplier in fluid flow communication with the burning zone for supplying oxygen for fuel combustion, a cooling jacket integrated in the body and cooling the burning zone independently of the air supplier, the burner being operable to release hot combustion gases into the combustion chamber, and a heat exchanger in the housing capturing heat from the hot combustion gases and transferring the heat to another medium.
In accordance with another aspect of the present invention, there is provided a burner comprising a body defining a burning zone having an area of greater burning and an area of lesser burning, an air supplier in fluid flow communication with the burning zone supplying oxygen for fuel combustion, a fuel feeder in communication with the burning zone supplying a renewable fuel source directly into the area of lesser burning of the burning zone.
In accordance with a further aspect of the present invention, there is provided a method of operating a furnace comprising a heat exchanger and a burner, the method comprising the steps of providing a burner having an air supplier and a cooling jacket, the air supplier and the cooling jacket being independently fed, determining a maximum and a minimum temperature for the heat exchanger and for the burner, determining an actual temperature in the heat exchanger and in the burner, controlling the air supplier and the cooling jacket independently thereby moderating the actual temperature in the heat exchanger and in the burner relative to the respective maximum and minimum temperatures.
Reference will now be made to the accompanying drawings, showing by way of illustration a particular embodiment thereof, and in which:
Referring to
The furnace 10 further comprises a burner 32 positioned inside the combustion chamber 14 adjacent the rear wall 18 of the housing 12 and racing the front door 26 thereof. More particularly, the rear wall 18 of the housing 12 includes an aperture 34 proximal to the floor 24 shown covered by a back wall plate 36, which is used for mounting the burner 32 in the furnace 10. Particularly, the burner 32 is fixed to the back wall plate 36 as will be described in detail furtheron, and is subsequently inserted through the aperture 34 of the rear wall 18 such that the back wall plate 36 is fixed thereto. The burner 32 can then be accessed by way of the front door 26 of the furnace 10.
The burner 32 is adapted to burn fuel pellets such as corn kernels or other cereals, or wood pellets to name a few renewal fuel sources. As the fuel burns, it generates hot combustion gasses which arc released into the combustion chamber 14 of the furnace 10. The furnace further comprises a heat exchanger 38 disposed in the housing 12 to capture the heat from the hot combustion gasses in the combustion chamber 14 and transfer the heat to another medium such as air or water, which is then used to heat an enclosure such as a building or the like.
In the exemplary embodiment illustrated in
Furthermore, the furnace 10 includes a pump (not shown) for circulating a flow of water in through the reservoir inlets 50 and out through the reservoir outlet 52. In greater detail, the flow of water travels upwards between the side and upstanding walls 20 and 54 through the passageways 56 and then between the top and bottom walls 44 and 46 about the tubes 40 before exiting through the reservoir outlet 52. Advantageously, the water traveling upwardly through the passageways 56 cools the side walls 20 of the housing 12 before being heating by the hot metal tubes 40. The heated water in the reservoir 42 is then transported through a piping system (not shown) and subsequently used to heat a building or the like.
In another example not illustrated, the heat exchanger 38 may include curved metal tubing disposed in the combustion chamber 14 through which air is passed therethrough. The metal tubing surfaces are heated by the upward flow of hot combustion gasses such that the air passing through the tubing absorbs heat from the hot metal surfaces. The heated air is then circulated through air ducts for distribution throughout a building or the like.
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In the exemplary embodiment illustrated in
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It can be seen that the fuel feeder 96 of the burner 32 is positioned near the floor 70 thereof so as to push fuel pellets into the burning zone 58 rather than drop same from an elevated position. During operation, the fuel feeder 96 transports the fuel pellets into the burner 32 through the second fuel feeder receiving opening 88. As the fuel pellets build up near the opening 88, the incoming fuel pellets push the accumulated fuel pellets towards the front of the elongated body 57 of the burner 32 thereby defining a longitudinal feeding direction 107. As the fuel pellets continue to accumulate in the burner 32, they form a hill-like formation that rises and expands as more and more fuel pellets arc introduced into the burner 32. The dimensions of the elongated body 57 and the volume of fuel pellets and speed at which they are delivered into the burner 32 are pre-determined to ensure that the hill-like formation of fuel pellets is built up in the burning zone 58 of the burner 32. Furthermore, the fuel feeder 96 is controlled by a control system (not shown) that can moderate the fuel flow thereby permitting continuous, sporadic or no fuel flow into the burner 32.
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It should be pointed out that the oxygen supplying means is separate from the cooling jacket 93 such that the latter can continue to cool the burner 32 even if the flow of air through air inlets 120 is cut off. A control system (not shown) independently controls both the oxygen supplying means and the flow of water in the cooling jacket 93. Also, it can be seen from
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Furthermore, the front door 74 of the burner 32 is located above the front walls 60, 62 thereof opposite the fuel feeder 96 disposed in the rear wall 68. An opening 126 is present in the front end of the burner 32 between one of the top covers 72 and the front door 74. The front door 74 is angled inwardly towards the rear wall 68 of the burner 32 for redirecting the flames upwardly, partly through opening 126. The front door 74 is removable or openable to provide readily available front access to the interior of the burner 32, thereby facilitating cleaning thereof. As previously mentioned the front door 74 of the burner 32 faces the front door 26 of the furnace 10 for easy access.
In the case of using corn kernels as fuel, the formation of unburned carbon structures commonly referred to in the industry as clinkers need to be removed from the burner 32. Therefore, the front door 74 permits quick and easy access to the inside of the burner 32 for removal thereof. Furthermore, the top covers 72 increase the temperature in the burner 32 which in turn helps increase the maximum energy (BTU) output for a given size burner while also helping to minimize the formation of ash and clinkers. Still further, the cooling jacket 93 integrated in the elongated body 57 of the burner 32 keeps the inner walls 60 and 64 cool thereby preventing the clinkers from sticking thereto.
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Moreover, a control system (not shown) as previously mentioned is used to control the furnace 10. For example, the control system can be controlled at a distance by a thermostat that can moderate the temperature in a given enclosure such as a room of a house. The control system determines the temperature in the furnace reservoir 42 and in the burner 32 by way of the previously mentioned sensors and subsequently controls the burner 32 output and the furnace 10 output as a whole according to the respective temperatures. The control system independently controls: the flow of water in and out of the reservoir 42, the flow of water in and out of the cooling jacket 93 of the burner 32 as well as the flow of air released into the burning zone 58 for combustion, and the flow of fuel into the burning zone 58.
A method of operating the furnace in accordance with a particular embodiment of the present invention is described below. A pre-determined minimum and maximum temperature is set for the reservoir 42 and for the burner 32. The temperature of the reservoir 42 and the temperature in the burner 32 is determined by the respective sensors and the information is supplied to the control system. If the temperature in either the reservoir 42 or the burner 32 is less than the respective minimum pre-determined temperature, then the control system goes into heating mode. If the temperature in either the reservoir 42 or the burner 32 is greater than the respective maximum predetermined temperature, then the control system goes into standby mode. When in heating mode, the control system is programmed to allow the fuel feeder 96 to continuously feed fuel pellets into the burning zone 58 at a predetermined speed. When in standby mode, the fuel feeder 96 sporadically feeds fuel pellets into the burning zone 58 thereby providing a minimum amount of fuel to maintain the fire burning.
More particularly, if the temperature in the reservoir 42 is less than the respective minimum pre-determined temperature, the flow of water through the reservoir 42 inlets 50 is reduced to prevent condensation from forming on the walls of the furnace 10 which would lead to ash sticking thereto. If the temperature in the burner 32 is less than the respective minimum predetermined temperature, the pump providing water flow into the cooling jacket 93 is stopped. If the temperature in the burner 32 is greater than the respective maximum pre-determined temperature, the pump providing water flow into the cooling jacket 93 is started. Notably, the control system may include an alarm to notify if the lire in the burner 32 is extinguished. In such a case, the control system is programmed to stop the fuel feeder 96 completely.
Therefore, it can be seen that the burner 32 can continue to be cooled even if the oxygen supply means supplying air into the burning zone 58 is completely shut down. Furthermore, the fuel feeder 96 is independent from both the cooling and aeration systems of the burner 32. And the cooling system of the burner 32 is independent of the reservoir 42 of the furnace 10.
It is within the ambit of the present invention to cover any obvious modifications of the embodiments described herein, provided such modifications fall within the scope of the appended claims.
Number | Date | Country | Kind |
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2,566,822 | Nov 2006 | CA | national |