Not applicable.
Not applicable.
Not applicable.
The invention relates to a solid fuel burning unit, by which the heated air, hot water, steam, and hot oil demands are met by burning coal, organic fuel, bagasse, nut shell, wood flour, rice stem etc. solid fuels, which are burned in industrial and domestic areas for production or heating purposes.
The present invention relates to a solid fuel burning unit comprising a fuel supply chamber wherein the fuel to be sent for combustion to the combustion region found in the body is placed and the feed mechanism carrying the solid fuel found in the said chamber forward, a main burning block having fuel/air cell connected to the said solid fuel supply chamber and air outlet vents formed on the external wall surface. A preventive surface positioned on the said main burning block external wall surface in a way that it would form a closed volume in a certain distance. At least one fuel discharge outlet provides sending of the fuel, which is transferred to the said main burning block cell, to the external wall surface. At least one push flap is provided, which provides pushing of the solid fuel to the outlet hole via the spiral wings formed as facing each other, and which is connected on the same shaft in a way that it would make rotating motion.
Nowadays, there are various types of burning techniques and heat rooms. Various deficiencies are encountered in most of these systems. For example, it is generally seen that volatile gases can not be combusted, required emission standards can not be met, and thus natural gas etc. fuels are preferred in classical burners. In the prior burners, high calorie coal is used due to inefficient combustion. However, its consumption is prohibited because its reserves are quickly exhausted and low calorie coal, which is easy to produce, can not meet the emission standards.
With the affect of the gases discharged from chimneys, flue dust is seen in pipes and halts are required in the facility or system for cleaning fire room pipes. Investment for filtration and dust holder cyclones are required in order to meet the emission standards. When the un-combusted carbon ratio of the ash examination after combustion in the prior combustion techniques (stoker, fluid bed, traveling grate, manual load etc.) is analyzed, they are observed to operate at around a 30-70% efficiency level.
Since excessive fuel load is made in the prior systems, and due to the CO found in the chimney emission, a high amount of losses occur or stack gas losses occur due to burning low amount of coal with high rate of air. In some burner systems, coal thickness is so high in some areas (formation of CO increases due to insufficient air) and so low in other areas (causes excessive air and increase of oxygen amount in the stack gas). Coal is not spread uniformly in the medium where it is combusted, and therefore the stack gas analysis show high oxygen and CO ratios at the same time.
Efficiency of the burner is affected by air amount, uniformity, proportionality, homogeneous spreading, and controllability of the system and these conditions can not be achieved in the prior systems. In many combustion systems, it is seen that the air amount is simply adjusted according to the appearance and way of burning of the coal. Most of the classical burners are picky about fuel. They can combust only certain sizes of fuels and high dust level affects combustion efficiency in the classical burners and also many systems are not convenient for burning dust or they simply can not burn. In coarse coal burners, efficiency is low, since the optimization of spreading of the coal is not uniform and the dust ratio is variable.
In general applications, feed controls are adjusted in a faulty manner and stack gas losses reach very high levels due to excessive air. Systems providing air/fuel control are fitted to large capacity fire rooms and in this way the efficiency of fire rooms attempts to be improved. However, the burning and operation technique of these systems are not efficient enough, they have high costs and their first investment costs are also very high.
At the hotspot (fire rooms) region of the prior systems, water walls, air walls etc. systems are used instead of insulation. This approach cools the fire room and the temperature of the hotspot becomes much lower than the ignition temperature of solid fuels and thus efficient combustion can not occur.
Some applications are encountered in the patent research made about fuel systems. Among these applications, a patent application is found with No. TR2004/01312 and dated Jun. 4, 2004. On the abstract page of this application, these expressions are found: The present invention relates to having barrel-shaped corresponding nozzles at the metal surface facing the fire of coal burning chamber of the coal burning system (stoker), placement of firebricks at the metal surface in a way that they would also close the nozzles, passing of the shaft, which provides coal feed, into the coal burning chamber through a narrow mouth, and thermostatic protection. There are nozzles at the metal surface facing the fire of the coal burning chamber and the metal surface is covered with firebricks. Coal brought to the narrow mouth coal burning chamber by the shaft is heated with the heat given from the nozzles. When the fire room is not active, the thermostat locks the system and prevents air flow.
Another application is No. TR2002/01980, application of which was made to Turkish Patent Institute on Sep. 8, 2002. In this application: the invention is a system formed of reducer, coal chamber, spiral pipe, fan, air pipe, combustion room, time limit relay, thermostat, and by-pass pipe in order to provide high efficiency, environmentally friendly, and automatic combustion of 10-18 mm nut-coal in solid, liquid, and gas fuel heating boilers.
In another application with No. TR2003/01675: the invention is formed of combustion device, burning tube, conic-shaped spiral, movable fuel valve, and movable slag crusher grits. Fuel valve and conic spirals are driven by an engine reducer and the movable grit and slag crusher system is driven by a hydraulic power source connected to cylinder piston mechanism. Grit and slag crushers are connected to a shaft passing through the beds placed near the tube. The flush valve is placed at the head part of the tube in a shape and position that it would flush the fuel found in the chamber above itself onto the spirals.
In the application with No. TR2009/07257: the invention relates to vertical push coal burning system, which can be applied in hot air boilers, heating boilers, high pressure steam boilers, and hot oil boilers, which can both combust coal and dust, and which implements efficient combustion as a result of mixing the coal during combustion via the pushing part found in the system.
A purpose of the invention is to have different technical features than the prior art systems bringing a novel development in the field. The present system operates with 97% combustion efficiency. Moreover, it provides combustion of volatile gases originating from coal and obtaining energy from these gases.
A purpose of the invention is to provide combustion of 2000-7500 kkcall coal in sizes between 0-10 mm, 10-30 mm, and 30-50 mm and rate of moisture below 15%.
Another purpose of the invention is to have a system operating continuously and efficiently between 10-100% interval capacities with its original combustion structure. It responds to any possible capacity increase or decrease in the system easily with the same efficiency.
Another purpose of the invention is to produce this combustion system in larger and smaller sizes and capacities according to demand starting from domestic heating.
Another purpose of the invention is to provide an aerodynamic form with a circular burner, cylindrical combustion room, and dome-shaped roof. Also, the mechanical strength of the refractory material extends the operating life.
Another purpose of the invention is to minimize the energy losses by radiation, contact, and conventional ways with the refractory design.
Another purpose of the invention is to have a burner system providing homogeneous coal and air mixture on the entire surface.
Another purpose of the invention is to have special refractory cell providing combustion of volatile gases.
Another purpose of the invention is to eliminate the need for dust holding cyclone, recovery systems etc. additional equipments by recovering the gases via being combusted in the burner system, and thus not to bring additional cost.
Another purpose of the invention is to obtain optimum burning efficiency regulating stack gases and chimney temperature by continuously controlling the fuel and the oxygen.
Another purpose of the invention is to have a coal spreading system. Coal and air mixture is homogeneous. And this property is a factor of the burning efficiency.
Another purpose of the invention is to obtain an environmentally friendly system by achieving burning efficiency and minimizing particle ratio in the chimney.
Another purpose of the invention is to have an automatic slag crusher and discharge system as another advantage of the combustion system. In this way, its burning efficiency is maintained, provides endurance, does not require an operator, provides healthy and clean operating environment, and does not need halting due to slag and ash.
Another purpose of the invention is to minimize halting and failure by examining failure and maintenance points. Way of operation is simplified and operation software is developed using PLC. Since it is extremely easy to operate and operated by automation, operator error is eliminated. It provides continuous and optimum efficiency.
In order to achieve the above said purposes, the invention relates to solid fuel units comprising a fuel supply chamber wherein the fuel to be sent for combustion to the combustion region found in the body is placed and the feed mechanism carrying the solid fuel found in the said chamber forward. It comprises a main burning block having fuel/air cell connected to the said solid fuel supply chamber and air outlet vents formed on the external wall surface, a preventive surface positioned on the said main burning block external wall surface in a way that it would form a closed volume in a certain distance, at least one fuel discharge outlet providing sending of the fuel, which is transferred to the said main burning block cell, to the external wall surface, and at least one push component, which provides pushing of the solid fuel to the outlet hole via the spiral wings formed as facing each other, and which is connected on the same shaft in a way that it would make rotating motion.
In
The invention relates to the solid fuel units (200) comprising a fuel supply chamber (100) wherein the fuel to be sent for combustion to the combustion region found in the body (10) is placed and the feed mechanism (30) carrying the solid fuel found in the said chamber (100) forward. It is characterized in that it comprises a main burning block (20) having a fuel and air cell (22) connected to the said solid fuel supply chamber (100) and air outlet vents (21) formed on the external wall surface (28), and a preventive surface (50) positioned on the said main burning block (20) external wall surface (28) in a way that it would form a closed volume in a certain distance.
The invention comprises at least one fuel discharge outlet (23) providing sending of the fuel, which is transferred to the said main burning block (20) cell (22) as seen in
The said fuel feed mechanism (30) seen in
The invention also comprises a fuel spreader and mixer (40) seen in
On the said preventive surface (50), the invention comprises an impact surface (51) seen in
The invention comprises a combustion cell (53) formed by positioning of the said positioning feet (52) on the load bearing feet (60), an air supply fan (120) having an air transfer line (121) providing external air support to the said main burning block (20) air inlet hole (27) and connected to this air inlet hole (27), an ash removal line (13) in connection with the body (10), to which the fuel ashes are transferred, and having a transfer duct (114), an ash removal mechanism (110) having a spiral of advance (111) and conveyor outlet (113) discharging the ashes coming from the said ash removal line (13), a drive component (112) providing rotating motion to the said spiral of advance (111), and a slag crusher component (130), which provides crushing of the slags falling in the said transfer line (13), and which is positioned in this line (13), and the said slag crusher component (130) comprises crusher wings (131) and bedding components (132).
The invention comprises at least one pressure gauge (150) positioned on the body (10) in order to gauge the pressure inside the said solid fuel unit (200) and comprises refractory insulation (90) positioned at the inner surface of the said body (10). A hot cell (11) surrounded by refractory insulation (90) and hot water and/or liquid pipes (80) positioned in this hot cell (11) are formed and also body feet (12) are formed at the body (10) lower region. The invention comprises chimney outlet (70) for discharging the stack gases formed in the hot cell (11), conic surfaces (71) formed at the region of this chimney outlet (70) extension facing the inside of the body (10), and viewing windows (140) again formed on the body (10) outer surface.
The operation system of the unit (200) is as follows: There is a metal body, in which all the structures are found, and which provides bearing of the unit. In order to enable intervention from below, the body (10) is found on feet (12).
Body (10) is cylindrical, while the roof is in a dome-form. Not to mention the fact that, the chimney is placed at the center of the dome. This aerodynamic form increases the burning performance. Integrity is given to the combustion cell with its burner shape. This form also provides mechanical strength for the refractory insulation (90).
There is a drive component (31) of the fuel feed mechanism (30) (drive component is an engine and reducer). Fuel is taken from the fuel supply chamber (100) with the help of the driven spiral wings (32). At the same time, air is given to the combustion cell (53) from the combustion block (20) air outlet vents (21) via the air supply fan (120). Solid fuel taken from the feed chamber (100) is transferred to the burner hole (23) via the spiral wings (32, 33). Counter-force is formed when the fuel encounters the inverse spiral wing (33) and it is transferred upwards, or in other words, towards the fuel discharge outlet (23) with the impact of the push component (34) operating on the spiral shaft. While the fuel moved by being compacted among the spirals (32, 33) goes towards the combustion surface, or in other words, towards the external wall surface (28), its volume expands while going through the oval surfaces (29.1) of the conic surface (29). With this expansion, heat transfer to the fuel is made quicker. This function provides heating of volatile gases found in the fuel while they go up to the burner radiused surfaces (24) and provide removal of the volatile gases found in the fuel. Feeding of the solid fuel from the burner centre provides homogeneous and uniform solid fuel exit to the combustion surface of the main burning block (20) radiused surface (24). Radiused surfaces (24) play an effective role in homogeneous and uniform spreading. Fuel spreader and mixer (40) provide homogeneous spreading of the fuel with volatile gases removed on the burner radiused surface (24).
From the air holes spread all around the burner surface in a certain system in accordance with its capacity, the air demanded by the burner is homogeneously transferred to the entire surface. This kind of spreading enables homogeneous combustion on the entire surface and increases efficiency. Volatile gases and combustible sulphur, which are removed from the structure, hit the preventive surface (50) made of refractory material while advancing in the burner hole and pass through the flame trap spread all over the surface and volatile gases are combusted in this way. Fuel fed on the burner continuously and in a controlled manner moves in accordance with the circular and swaged surface of the burner and proceeds by being combusted with the impact of the fuel spreader and mixer and air outlet vents (21) and the carbons found within it combust and turn into ash. The ashes and the slag are transferred to the ash removal mechanism (110) found below providing easy discharge of the ashes and the slags. In order to provide easy intake of the formed slag in pieces, herringbone cross partitions (25) are found on the radiused surface (24). Slags are manually interfered via combustion viewing and slag interference hole and thus they are sent to the conveyor outlet (113). While slag is poured into the chamber from the fuel, it is crushed in the crusher component (130) and removed from the unit (200) by being removed from the ash chamber via the spiral of advance (111).
Number | Date | Country | Kind |
---|---|---|---|
2010 05272 | Jun 2010 | TR | national |
Number | Name | Date | Kind |
---|---|---|---|
923404 | Burger | Jun 1909 | A |
1392323 | Goldberg | Oct 1921 | A |
2320410 | Cheasley | Jun 1943 | A |
2455817 | Sherman | Dec 1948 | A |
3693812 | Mahr et al. | Sep 1972 | A |
4540467 | Grube et al. | Sep 1985 | A |
5027719 | Chenard | Jul 1991 | A |
5052311 | Kincaid | Oct 1991 | A |
5382291 | Olioso | Jan 1995 | A |
5507946 | Stearns | Apr 1996 | A |
Number | Date | Country | |
---|---|---|---|
20110315056 A1 | Dec 2011 | US |