REACTOR CAPABLE OF CARBONIZED DRYING AND BURNING VOLATILE GASES TOGETHER WITH TOXIC GASES

Abstract

A solid-fuel burning and drying unit capable of carbonized drying and burning of toxic gases, having a main body with a fuel cell configured in the main body, a barrier surface which closes the fuel cell from the upper region and enables combustion of toxic and volatile gases in the combustion zone without mixing with the atmosphere, fuel supply elements and fuel discharge elements that deliver fuels to be burned into the fuel cell, wherein the said main body contains a drying unit in which the damp fuel is dried by heat from the combustion zone by generating frictional energy by rotating through the configured drive element and coils on the axis of rotation (z).

Claims

1. A solid-fuel burning and drying unit capable of carbonized drying and burning of toxic gases, having a main body comprising a fuel cell configured in the said main body, flue gas cavities providing flue gas outlet towards an outer wall of an upper zone dome structure, a barrier surface which closes said fuel cell from the upper region and enables combustion of toxic and volatile gases in a combustion zone without mixing with the atmosphere, fuel supply elements and fuel discharge elements that deliver fuels to be burned into the fuel cell, wherein the said main body contains a drying unit in which the damp fuel is dried by heat from the combustion zone by generating frictional energy by rotating through the configured drive element and coils on the axis of rotation (z).

2. A solid fuel burning and drying unit according to claim 1, comprising a drying unit having a solid fuel mixer main shaft, where rotational motion is generated by at least one motor reducer, and a friction surface that turns damp fuel by means of coils configured on this solid fuel mixer main shaft.

3. A solid fuel burning and drying unit according to claim 1, comprising a particle collection zone where the right amount of suction is done to a particle evacuation outlet and the particles in the drying unit are discharged by means of a discharge tube.

4. A solid fuel burning and drying unit according to claim 1, wherein, the said drying unit comprises sidewalls with conical surfaces and a particle impact screen that allows the passage of particles to the particle collection zone.

5. A solid fuel burning and drying unit according to claim 1, comprising the hot air in the access channel to the drying unit is connected with a T connection and contains the flue gas pipe which allows the hot air to be circulated.

6. A solid fuel burning and drying unit according to claim 1, comprising a drying unit Inlet which allows the transfer of moist solid fuel from any bunker other than the fuel to be dried to the drying unit.

7. A solid fuel burning and drying unit according to claim 1, wherein, the said drying unit comprises at least one steam suction line, a steam collection and discharge pipe, and at least one steam outlet, which allows the said steam to be delivered to the outside environment and/or to the line where the steam will be used.

8. A solid fuel burning and drying unit according to claim 1, comprising a drying unit bearing at the same rotation axis (z) and at the same center of the main body and moving from the same drive element.

9. A solid fuel burning and drying unit according to claim 1, comprising a drying unit in which three effective drying is done with the effect of heat from a Hot Zone and hot air from the flue gas outlet and the rotational and frictional effect created by means of coils.

10. A solid fuel burning and drying unit according to claim 3, comprising particle side walls in which the particles are oriented with the force of the center with the rotational effect during the flue gas passage in the said drying unit.

11. A solid fuel burning and drying unit according to claim 1, comprising at least one access channel to the drying unit, and this access channel, a discharge fan, a flue gas fan motor and a transfer pipe which absorb 900° C. flue gas from the combustion chamber, and transport the flue gas to the drying unit.

12. A solid fuel burning and drying unit according to claim 2, comprising a fuel cell in the upper part of the temperature formed in the combustion zone at 1800° C., and the base sheet from which the heat generated in the flue gas hot zone of 900° C. is transferred.

13. A solid fuel burning and drying unit according to claim 1, comprising a temperature sensor which is activated and the dry solid fuel is discharged to the outside via the fuel discharge outlet, when the moist solid-fuel internal temperature of the product to be dried reaches 105° C.

14. A solid fuel burning and drying unit according to claim 1, comprising a coil which allows transport to the drying unit, and the fuel transport pipe, the propulsion element and the discharge pipe which provide rotational movement to the said coil.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0029] FIG. 1 is the general perspective view of the reactor of the invention.

[0030] FIG. 2 is the section perspective view of the reactor of the invention.

[0031] FIG. 3 is the section perspective view of the reactor of the invention from a different angle.

[0032] FIG. 4 is the top view of the blocking surface of the burning zone in the reactor of the invention.

[0033] FIG. 5 is the cross-sectional perspective view of the ash-collecting zone of the reactor of the invention from the top.

[0034] FIG. 6: Close-up exterior elevation perspective view of the drying unit of the invention.

REFERENCE NUMBERS

[0035]

TABLE-US-00001    1. Burning and drying unit  2. Fuel cell  2.1-Combustion air feeding tube  2.2-Combustion air vent holes  3. Ash discharge cone  4. Blocking surface  4.1 Bedding zone  5. Reflector material (fired brick)  6-Hot Zone  7-Combustion zone  8-Particle collection zone  8.1 Particle discharge pipe  8.2 Particle discharge outlet  8.3-Open area with particle impact screen  8.4-Particle side wall  9-Bearing feet 10-Drying unit 11 -Coil 11.1-Drying unit inlet 12-Main shaft of solid fuel mixer 13-Engine reducer 14-Flue gas pipe 15-Access channel to drying unit 15.1-Discharge fan to the drying unit 15.2-Flue gas fan engine 15.3.-Transport pipe 16-Friction surface 16.1 Side walls 16.2. Bottom plate 17-Temperature sensor 18-Bunker 19-Fuel transport pipe 19.1-Coil 19.2-Discharge pipe. 20-Fuel discharge outlet 20.1-Discharge pipe. 21-Propulsion element 22-Steam collection and discharge pipe 23-Steam outlet 24-Steam suction line 25-Ash discharge line 25.1-Ash discharge pipe and apparatus 26-Ash discharge engine group 27-Incineration air provider 28-Fuel dispatch main engine 29-Fuel supply drive unit 30-Main Body 31-Fuel supply transport line 31.1-Conical coil line 32-Slag crusher unit 33-Conical coil 34-Fuel transport shaft 35-Flue gas cavities 36-Combustion cell peepholes 36.1 Combustion cell cover 37-Flue gas transition gap Z-Axis of rotation

DETAILED DESCRIPTION OF THE INVENTION

[0036] The solid fuel burning and drying unit (1), shown in FIG. 1, is capable of drying by carbonizing and burning the third gas together with the toxic gases. In general, it has a main body (30), comprising a fuel cell (2) configured in the said main body (30), flue gas cavities (35) providing flue gas outlet towards the outer wall of the upper zone dome structure, a barrier surface (4) which closes said fuel cell from the upper region and enables combustion of toxic and volatile gases in the combustion zone (7) without mixing with the atmosphere, fuel supply elements and fuel discharge elements that deliver fuels to be burned into the fuel cell. The said fuel cell (2) also contains the combustion air supply tube (2.1) and the combustion air vent holes (2.2). The system also includes an ash discharge cone (3), ash discharge line (25), ash discharge pipe and apparatus (25.1), ash discharge engine group (26), incineration air provider (27), fuel dispatch main engine (28) and fuel supply drive unit (29).

[0037] The combustion and drying unit (1), shown in FIG. 2, as its inventive feature comprises a drive element configured on the main body (30) and a drying unit (10) which rotates by means of augers (11) in the rotation axis (z) and generates frictional energy and dried the heat and moist fuel coming from the hot zone. The drying unit (10) has a solid fuel mixer main shaft (12), where rotational motion is generated by at least one motor reducer (13), and a friction surface (16) that turns damp fuel by means of coils (11) configured on this solid fuel mixer main shaft (12). The said drying unit (10) includes sidewalls with conical surfaces (16.1) and a particle collection zone (8) with particle impact screen (8.3) that allows the passage of particles to the particle collection zone (8) seen in FIG. 5 and a particle collection zone (8) where the right amount of suction is done to the particle evacuation outlet (8.2) and the particles in the drying unit (10) are discharged by means of the discharge tube (8.1) shown in FIG. 1. In the reactor combustion zone (7) flue gas fan suction pipe (FIG. 1) also has a flue gas pipe (14) where hot air is connected by a T connection and allows hot air to circulate. The combustion and drying unit (1) has bearing feet (9).

[0038] On the other hand, for the fuel to be dried, the bunker (18) in FIG. 1, the fuel cell (2) in the bunker (18) in FIG. 3 that show the solid fuel that comes with the fuel supply transport line, as well as the fuel cell (2) fed through a conical coil line, the heat energy obtained by the fuel is available. The central shaft of the reactor from the combustion chamber in 900° C. flue-gas drying unit (10) to the drying unit transition line (15) provides the transportation of the flue gas to the drying unit, under 900° C. from the combustion chamber to the drying unit by absorbing the flue gas discharge fan (15.1) and flue gas fan motor (15.2) provides. This structure also contains a transport pipe (15.3) (see FIG. 6). It contains the coil (19.1) which allows transport to the drying unit (10), and the fuel transport pipe (19), the propulsion element (21) and the discharge pipe (19.2) which provide rotational movement to the said coil. In addition, the said drying unit (10) contains at least one steam suction line (24), a steam collection and discharge pipe (22), and at least one steam outlet (23), which allows the said steam to be delivered to the outside environment and/or to the line where the steam will be used.

[0039] The operation of the combustion and drying unit (1) in FIG. 3 is as follows; the fuels transferred to the fuel cell (2) by means of the fuel supply transport line (31) are subject to combustion from this region. By means of the barrier surface (4) having the bearing region (4.1) in the fuel cell (2), the fuels are burned together with the volatile and toxic gases with an emission close to zero. The blocking surface (4) and fuel cell (2) are surrounded by the reflector material (5). Just above the hot zone (6), there is the particle collection zone (8) and above it, there is the drying unit (10). The fuel supply transport line (31) also has a conical coil line (31.1). On the other hand, the conical coil (33), the fuel transport shaft (34), the flue gas cavities (35), the combustion chamber peepholes (36), the combustion chamber cover (36.1) and the flue gas transition cavity (37) is integrated into the system.

[0040] The mode of operation of the drying unit (10) is as follows; the fuels to be dried into the drying unit (10) are supplied from any outside supply bunker to the moist solid fuel drying unit (11.1). The fuel to be dried in the drying unit (10) is subjected to rotational effect in this area. The moist fuel to be dried by transferring the blades of the solid fuel mixer main shaft (12) in the rotation axis of the coil (11) during rotation will be continuously rotated in this area. The material (moist fuel) is taken from the bottom to the top and the fuel to be dried is constantly mixed. Furthermore, the high temperature from the lower hot zone (6) to the environment is provided by the bottom plate (16.2). This environment is oxygen-free environment. Its transfer by means of the coil (11) also creates a frictional effect. Accordingly, a temperature is formed by friction in the oxygen-free environment. Also, 900° C. provides drying as the flue gas passes through the drying unit. When the moist solid-fuel internal temperature of the product to be dried reaches 105° C., the temperature sensor (17) is activated and the dry solid fuel is discharged to the outside via the fuel discharge outlet (20). The benefits of the fuel discharge output (20) are clearly evident when delivering high-calorie high-quality, dehumidified solid fuel to a sack or a tractor or trailer and obtaining energy, as well as recycling and disposing of 100%. During the discharge of the dried solid fuel to the drying unit by the propulsion of the propulsion element (21), the dried fuel is discharged by the discharge pipe (20.1) to the fuel supply body and the dried fuel is discharged by the discharge outlet (20).

[0041] At the same time, the transition channel from the flue gas outlet to the drying unit (15) via the flue gas pipe (14) is given into the hot air drying unit (10), which is received through a T pipe. The steam generated here is given out by means of the steam suction line (24) and steam outlet (23). Or it is possible to transport steam through pipes to a region where steam is needed.

[0042] During the passage of flue gas in the drying unit (10), the particles are oriented towards the corner of the side walls (8.4) with the force of the center by the rotational effect, and through the open field with the particle impact screen (8.3) and the material weight, the particles fall from this screen opening area to the particle collection zone (8). Particles falling in this zone are evacuated to the exterior zone via the discharge pipe (8.1) and a suction line and the particle discharge outlet (8.2).

[0043] The drying unit (10) has a structure bearing the same rotation axis (z) and the same main body (30) center and moving from the single drive center. At the same time, together with the heat from the hot zone (6), the rotational and frictional effect created by the coils (11), and the effect of the hot air from the transition line (15) to the drying unit, it has a superior drying feature where a three-times effective drying is performed.

[0044] The drying unit (10) of FIG. 2 rotates the drying motor reducer (13) and the first factor, which consists of the mixing of the moisturized solid fuel mixer of the transfer coil (11), causes the solid fuel's core temperature to reach 50° C. The second factor is the heat transfer of the heat generated by burning solid fuel through the heating bottom plate (16.2) of the fuel cell (2) under the heat generated by the fuel cell (6) at the top of the fuel cell is 1800° C. and in the chimney gas hot zone at the bottom of the drying unit at 900° C. The third factor is that the solid fuel which is being installed due to the high temperature flue gas oxygen-free environment during mixing of solid fuel in an oxygen-free environment, which passes through the access channel (15) of the flue gas from the central cavity of the reactor combustion cell, does not burn and does not fire and does not present danger. 900° C. flue-gas of solid fuel in the drying unit during the drying, the heat energy 90% of solid fuel drying with flue gas in spent steam outlet pipe (chimney) 74° C. water to steam and exits as converted into automation control of agricultural land is to be used as irrigation water. By combining the three factors mentioned above, the drying process is provided with 90% lower cost than existing technologies. In addition, while the amount of dehumidification in solid fuels cannot exceed the maximum 15% in other current technologies, drying cost of the technology in our invention, which delivers 80% moisture reaching up to 7 times of the humidity of the current technology, it also lowers the max 15% dehumidification cost of the current technology by 80% via the carbonized drying process.

[0045] Thus, the heat energy obtained from the heat center sends the flue gas drying unit (10) to the drying unit transition channel (15) of the flue gas shown in an oxygen-free environment and the drying capacity is 750 kg/hour. In the test performed by the accredited laboratory, 750 kg/h drying the fuel in 1 hour and reducing it from 80% moisture to 2% moisture, dried solid fuel (Egg hatching manure) is 80% moist calorific value is 150 kg/Kcal is reduced to 2 humidity and increased to 3570 kg/Kcal, 1800 c ° combustion zone (7) by descending from 750 kg laying manure to 2% moisture, dry carbonized 3570 kg/kcal solid fuel is obtained at 165 kg/hour. 15% of the solid fuel dried by carbonization is used to obtain heat energy by burning in the reactor combustion zone (egg chicken manure), approximately 24.5 kg/hour solid fuel is burned to the fuel cell by obtaining heat energy by carbonizing the drying is carried out. The excess fuel obtained by 24.5 kg/hour solid fuel used by carbonized dried solid fuel (egg chicken manure) to obtain heat energy is 140.5 kg/hour. While the solid fuel with an economical value of 3750 kcal/kg is obtained, organic fertilizer which is an environmental disaster is 100% disposed of and converted to energy.