KR101326222B1 - The manufacturing apparatus of coal briquet using waste of efb(empty fruit bunch) - Google Patents

Abstract

The present invention relates to a coal briquette manufacturing apparatus using the waste of EFB (empty fruit bunch), comprising a crusher which crushes the waste of EFB; a pulverizing machine which pulverizes the crushed waste of EFB; a conditioned quantity supplier comprising a screw to supply the pulverized waste in a fixed quantity; a drier comprising a burner for drying the waste; a conditioned quantity supplier comprising a screw to supply the dried waste in a fixed quantity; a carbonizing basin heated by indirect heat, comprising a burner for carbonizing the waste at 400-450; a cooler which cools the carbonized material in multiple steps, and cooled by indirect heat; a mixer mixing a binder with the cooled carbonized material; a conditioned quantity supplier the comprising a screw to supply the mixed carbonized material in a fixed quantity; a molding device molding the mixed carbonized material; a separator separating the molded coal briquette from the mixed carbonized material; and a storage storing the coal briquette.

Description

The manufacturing apparatus of coal briquet using waste of EFB (empty fruit bunch)}

The present invention relates to an apparatus for producing coal briquettes of palm waste for use as an environmentally friendly fuel by carbonizing palm waste including fibrous palm fruits discarded after oil is collected.

The present invention provides a crusher for crushing farm waste, a pulverizer for crushing the crushed palm waste, a quantitative feeder composed of a screw for supplying pulverized palm waste quantitatively, and for drying the pulverized palm waste supplied in a quantitative manner. A dryer including a combustor, a metering feeder composed of a screw to supply dry farm waste in a quantitative manner, and a combustor for carbonizing the dried farm waste supplied in a quantitative manner at a high temperature (400 to 450 ° C.) and by indirect heat. A carbonized furnace to be heated, a cooler cooled in multiple stages of carbide carbide by high temperature and cooled by indirect heat, a mixer for mixing the binder with the cooled carbide, and a screw to supply the mixed mixed carbide in a fixed quantity. A fixed-quantity feeder, a molding machine for molding the mixed carbide supplied in a fixed quantity, and molded coal molded in the molding machine The present invention relates to an apparatus for producing coal briquettes using a farm waste comprising a separator for separating and mixing carbide and a reservoir for storing coal pellets.

Palms include coconut palms, pan palms, oil palms, and the like, and oil palms, date palms, and coconut palms are known as palms grown or grown in large quantities in Southeast Asia, the Middle East, Africa, and Latin America.

Until now, in the various kinds of farms, the fruits, stems, and leaves of the palms are discarded, and when the wastes are discarded, the fruits, stems, and leaves of the palms are incinerated or used as feed for livestock. There is a problem in that carbon dioxide gas increases in the atmosphere by incineration of farm wastes to the extent that it is legislated to incinerate farm wastes. In addition, when farm waste is incinerated, when used as feed, and used as compost, there is a limit in treating a large amount of farm waste.

As mentioned above, because of the environment of the tropics, the production of palm is fast, and since the waste of the palm is made of fiber, when the palm waste is carbonized, there is a property to obtain more pure carbide than the palm waste is converted to ash. Carbide composed of the same method can be used as an environmentally friendly fuel.

The present invention provides a quantitative feeder consisting of a crusher for crushing the farm waste to a certain standard, a pulverizer for crushing the crushed farm waste to a smaller standard, a screw for quantitatively supplying the pulverized waste quantitatively, Dryer for drying crushed farm waste at high temperature (150 ~ 350 ℃), fixed quantity feeder for supplying dry waste in fixed quantity, and carbonization furnace for carbonizing dried farm waste supplied in fixed quantity at high temperature (800 ~ 1000 ℃) A cooler for cooling the carbonized palm waste, a mixer for mixing the binder with the cooled carbonized palm waste, a molding machine for molding the carbonized palm waste (hereinafter referred to as mixed carbide) in which the binder is mixed, a molding molded in the molding machine A separator for separating coal and unmolded mixed carbide, a screw conveyor for transporting the mixed carbide to a mixer, and storing coal It aims to provide a manufacturing device for forming burnt with farm waste consisting of Django.

Palm waste to be applied to the present invention is applied to palm fruit by-products, palm leaves, palm stem, etc., and targets the biomass that can be applied to the present invention.

Shredder for shredding the farm waste according to the present invention is configured to cut the prototype of the farm waste to the size of 80 ~ 100mm.

The crusher blades of the crusher in order to increase the cutting force compared to the rotational force to be configured in a spiral on the rotation axis of the crusher, it is to be configured in a pair.

The pitch of the blade of the shredder is configured to be the same width as the size of the farm waste to be cut.

When the farm waste passes through the crusher, the cutting force can be increased by configuring to cut at the point where both spiral blades intersect.

The mill according to the invention is configured to cut the size of the crushed palm waste smaller in the crusher before the mill.

Palm waste is pulverized in the grinder is configured to be crushed to the size of 30 ~ 50mm.

As described above, when the farm waste shredded in the shredder is transferred to the grinder, a screw conveyor may be used to transfer the farm waste in a quantitative manner.

Palm waste that is transferred to the dryer to dry the pulverized farm waste as described above is to be transported in a quantitative manner.

As described above, the farm waste transported to the dryer is configured to dry while passing through the rotary dryer.

The dryer is configured to dry the farm waste of the dryer while the combustion gas of a high temperature (150 ~ 350 ℃) flows in front of the dryer to move to the rear of the dryer.

The dryer is composed of an inner cylinder and an outer cylinder so that the farm waste flowing into the inner cylinder is moved forward by a screw formed in the inner cylinder, and a portion of the moving farm waste is also moved out of the hole intermittently formed in the inner cylinder and the inner cylinder hole. The farm wastes that have been removed are formed to be moved forward by the screws of the outer cylinder so that they can be transported while drying in one barrel in duplicate.

 The fuel of the combustor that provides the heat of combustion to the dryer is configured to combust with a fuel capable of safe combustion so that no combustion residues remain during combustion or in the farm waste to be dried, and in which the emission of carbon dioxide can be restricted during combustion. To use.

The dryer configured as described above is configured to dry the water content of the farm waste within 20% when the farm waste passes through the dryer in 30 to 60 minutes.

The carbonization furnace for carbonizing the dried farm waste has a dryer-like structure.

The outer periphery of the carbonization furnace forms a high temperature gas jacket at a high temperature (800-1000 ° C.), and the high heat provided to the high temperature gas jacket is indirectly provided inside the carbonization furnace to carbonize palm waste in the carbonization furnace. do.

The cooler for cooling the carbide carbonized in the carbonization furnace is configured to cool the cooler indirectly by being covered with a coolant jacket on the outer periphery of the cooler.

It is configured to inject nitrogen gas which is an inert gas so that the carbide cooled in the cooler does not burn.

The mixer is configured to mix the cooled carbide together with a binder so as to have a condition for increasing the completeness of the molding when forming the carbide.

The molding machine is configured to mold mixed carbide flowing from the mixer while rotating in a twin axis.

The separator is configured to separate the coal briquettes and the unmolded mixed carbide conveyed from the molding machine, and the unmolded mixed carbide is transferred to the mixer again.

The coal briquettes passed through the separator are to be stored in a storage cell.

Nitrogen gas is injected to prevent combustion from occurring in the coal briquettes stored in the storage.

Since the manufacturing apparatus for carbonizing the farm wastes according to the present invention can be indirectly carbonized, carbides of higher quality can be obtained than carbonization by direct combustion, and a large amount of carbides can be obtained.

In addition, it is configured to prevent air pollution during the carbonization process, there is no damage to the environment, and there is an effect of regenerating energy using palm waste.

1 a is a carbonization apparatus of the present invention
1 b is a coal briquette device of the present invention
2 is a longitudinal sectional view of a crusher;
3 is a longitudinal cross-sectional view of the dryer
4 is a longitudinal sectional view of a carbonization furnace
5 is a structural diagram of a molding machine

The present invention provides a crusher 13 for crushing the farm waste 100, a crusher 14a for crushing the crushed palm waste 100, and a quantitative feeder 15a for quantitatively supplying the crushed palm waste 100. And, a dryer 12 for drying the crushed farm waste 100 supplied in a fixed amount, a quantitative feeder 15b for supplying the dry farm waste 100 in a quantitative manner, and the dried farm waste 100 supplied in a fixed quantity ) Is a carbonization furnace 11 for carbonizing indirect heat at a high temperature (800-1000 ° C.), coolers 16a, 16b, and 16c cooled by indirect heat, and a mill 14b for pulverizing the cooled carbide. A mixer 17 for mixing the binder with the pulverized carbide, a quantitative feeder 15c for quantitatively supplying the mixed carbides, a molding machine 18 for molding the mixed carbides quantitatively supplied, and a molding machine 18 A separator 19 for separating the formed coal briquettes 50 and the mixed carbide, and storing the coal briquettes 50 from the Is composed of a storage (35).

Figure 1a shows the carbonization device according to the present invention to the cooling device and the cross section of the cooling device to show the structure of the cooling device.

1B illustrates a coal briquette forming apparatus according to the present invention.

Figure 2 shows the structure of a crusher for crushing the circular farm waste.

Figure 3 shows the structure of the dryer for drying the pulverized farm waste by showing the dryer in a longitudinal section and a cross-section.

4 illustrates the structure of a carbonization furnace for carbonizing dried farm waste by showing the carbonization furnace in longitudinal section and in cross section.

5 illustrates a state in which coal briquettes are formed by the structure of a molding machine.

As shown in a of FIG. 1, the shredder 13 is configured to be integrally formed with the metering feeder 15a so that the shredded farm waste 100 is transferred in a predetermined amount.

The shredder 13 is constituted by twin shafts 40a and 40b as shown in FIG. 2, and spiral blades 41 are integrally formed on the shafts 40a and 40b, respectively. It is formed over the length, the blade 41 formed on the shaft (40a, 40b) forms a pitch (80 ~ 100mm), but the pitch at intervals of the cutting size (80 ~ 100mm) of the palm waste 100 Forming.

When the shredder 13 formed as described above rotates, the blades 41 of both shafts 40a and 40b are formed to rotate while crossing each other, and the farm waste 100 is cut at the point where the blades 41 cross. Since the cutting force is generated at the intersection point is configured to increase the cutting force compared to the rotational force.

In order to configure the farm waste 100 shredded by the shredder 13 to a smaller size, the shredded palm waste 100 is configured to be shredded into smaller sizes (30-50 mm) while passing through the grinder 14a. .

The grinder 14a is formed so that the farm waste 100, which is crushed and formed integrally with the metering feeder 15b like the shredder 13, can be transported quantitatively.

Since the grinder can be configured according to the environment and conditions of the workplace, the conditions of the grinder are not limited in the present invention.

The crusher 14a may be configured in connection with the crusher 13, and may be configured to dry and crush the crushed palm waste 100.

However, when the grinder 14a grinds the dry farm waste 100, there may be a problem that more power is required to grind because the grind object is dried.

Arrangement of the grinder 14a as described above can be selected and installed according to the conditions and environment of the working environment.

The farm waste 100 pulverized in the crusher 14a is formed to be quantitatively transferred to the dryer 12.

The dryer 12 is formed to rotate, and is composed of an outer cylinder 60 and an inner cylinder 61.

The crushed palm waste 100 introduced from the metering feeder 15b is formed to flow into the inner container 61.

Inside the inner cylinder 61, a screw 31a is formed so as to transport the farm waste 100 introduced into the traveling direction.

The screw 31a is not integrally connected and is formed in a shape in which an intermediate middle thereof is cut off and continues, and a plurality of holes 62 intermittently along the circumference of the inner cylinder 61 over the length of the inner cylinder 61. A portion of the farm waste 100 that is perforated and conveyed is formed to be discharged through the hole 62. That is, a part of the farm waste 100 passing through the inner cylinder 61 is formed to be discharged into the outer cylinder 60.

The inner wall of the outer cylinder 60 is formed with a screw 31b along the inner wall, and the screw 31b is not formed integrally like the inner cylinder 61 but is formed in a shape that is broken and continues to form the inner cylinder 61. It is formed to adjust the feed rate of the farm waste 100 of the farm waste 100 and the outer cylinder 60, and the palm waste 100 moves the inner cylinder 61 and the outer cylinder 60 while the inner cylinder 61 and the outer cylinder 60 ) Is rotated together, so that the farm waste 100 of the inner cylinder 61 is discharged to the outer cylinder 60 while the inner cylinder 61 and the outer cylinder 60 is rotated, and the palm waste 100 of the outer cylinder 60 is It is configured to operate to also flow back into the inner cylinder (61).

As described above, since the farm waste 100 is dried while moving the inner cylinder 61 and the outer cylinder 60, the drying time becomes longer, and the drying efficiency is increased.

The heat of combustion provided to the dryer 12 is directly introduced into the outer cylinder 60 at a temperature of about 150 to 350 ° C., and the incoming heat of combustion passes through the inner cylinder 61 to dry the farm waste 100 of the dryer 12. The exhaust heat is exhausted to the cyclone (25a), the dust is discharged downward from the cyclone (25a), the combustion heat passes through the condenser (24a), the moisture is condensed and discharged into the water, and the residual heat of drying (150 ~ 250 ℃) is a dryer ( It is configured to circulate to the combustor 23a which provides heat to 12).

The moisture removal of the condenser 24a is formed to condense moisture by the cooling water of the cooling water tower 26, and the condensed water is formed to circulate to the cooling water tower 26.

The combustion gas of the combustor 23a is configured such that complete combustion heat is provided as dry heat using a soft gas.

The farm waste 100 dried in the dryer 12 is configured to dry at a water content of about 20%.

As described above, the farm waste 100 dried in the dryer 12 is formed to be transported in a fixed quantity and introduced into the carbonization furnace 11.

The carbonization furnace 11 is configured in the same shape as the dryer 12 and is formed to rotate.

However, the scraper 29 is formed on the outer wall of the outer cylinder 70 of the carbonization furnace 112 so that slag generated from the heat of combustion provided on the outer wall of the outer cylinder 70 is attached to prevent the thermal efficiency from being lowered.

The slag separated by the scraper 29 is formed to be discharged in the downward direction of the carbonization furnace (11).

In addition, the heat provided to the carbonization furnace 11 is formed so that it may be provided to the outer wall of the outer cylinder 70, and the high temperature gas jacket 27 is covered by the outer wall of the outer cylinder 70. As shown in FIG.

The high temperature gas jacket 27 is fixed to the outside of the rotating outer cylinder 70 is formed to provide heat to the outer cylinder 70.

Heat of high temperature (800-1000 ° C.) is provided between the high temperature gas jacket 27 and the outer wall of the outer cylinder 70 configured as described above, so that the heat generated from the outer wall is high temperature (400-450). Is configured to provide heat.

As described above, heat is provided to the outer wall of the outer cylinder 70 and heat of the outer wall is provided by conduction and convection to the inside so that the farm waste 100 in the carbonization furnace 11 completely constitutes carbonization.

The high temperature (800-1000 ° C.) heat provided to the carbonization furnace 11 is provided in the combustor 23b, and the combustion material is formed to use a mixture of soft gas and preformed coal.

As described above, the residual heat (400 to 450 ° C.) of the heat provided to the carbonization furnace 11 is formed to circulate to the combustor 23b providing the combustion heat to the carbonization furnace 11 and the farm waste 100 in the carbonization furnace 11. The heat gas generated in this carbonization process moves to the cyclone 25b like the dryer 12, the dust is discharged from the cyclone 25b, and the high temperature (450 ° C) gas passes through the condenser 24b to remove moisture. The gas is again formed to circulate to the combustor 23b.

The combustion gas generated in the carbonization furnace 11 is formed to be used together with the tar and the binder removed from the condenser 24b by including the tar generated while the farm waste 100 is carbonized.

Palm waste 100 carbonized in the carbonization furnace 11 as described above is carbonized at a high temperature (400 ~ 450 ℃) is configured to be transferred to the cooler (16a).

Carbide 101 of the farm waste 100 transferred to a high temperature (400 ~ 450 ℃) is cooled to a temperature of about 250 ℃ while passing through the first cooler (16a), the carbide 101 cooled to 250 ℃ The carbide 101 cooled to 150 ° C while passing through the second cooler 16b is formed to cool to a temperature of about 80 ° C while passing through the third cooler 16c.

Cooling water jackets 28a, 28b, and 28c are formed outside the coolers 16a, 16b, and 16c to be cooled by the coolant flowing in and out of the cooling water tower 26.

Nitrogen gas from the inert gas tank 34 is optionally injected into the carbide 101 passing through the coolers 16a and 16b to prevent combustion.

The carbides 101 cooled by the coolers 16a, 16b, and 16c as described above are formed to be transferred to the grinder 14b using the screw conveyor 22a.

Carbide 101 pulverized in the crusher 14b is formed to be crushed to a size of 100 ~ 150 mesh.

The carbide 101 passed through the metering feeder 15c integrally formed in the grinder 14b is formed to be transferred to the mixer 17 in a fixed amount.

The mixer 17 is formed such that 3 to 5% of the binder is introduced into the binder tank 33 and tar and water formed in the carbonization furnace 11 are introduced to mix with the carbide 101.

As described above, the mixed carbide 102 mixed with the carbide 101, the binder, the tar, and the water is formed to have a water content of 5 to 8%.

The mixed carbide 102 mixed in the mixer 17 is formed to be transferred to the molding machine 18 in a fixed amount.

The size of the coal briquettes 50 formed in the molding machine 18 is composed of a size of 30 ~ 50mm.

As illustrated in FIG. 5, the molding machine 18 is configured to form the coal briquettes 50 while the rotating shafts of the twin shafts are engaged with each other to rotate.

The mixed carbide 102 flowing into the molding machine 18 is formed in the molding tool 51 in the process of being engaged with the rotating body of the molding machine 18, and the molding coal 50 is formed in the molding machine 18. It is formed to be separated.

As described above, the coal briquettes 50 separated from the molding machine 18 and the mixed carbide 102 that are not molded pass through the separator 19 while the coal briquettes 50 are discharged from the separator 19 to the conveyor 21. The mixed carbide 102, which is not transported and formed, is configured to be transferred back to the mixer 17 using the screw conveyor 22b.

Molded coal 50 formed as described above is formed to be stored in the storage 35, the storage 45 is also formed therein the screw plate 36 as shown in 2 to form the molding coal 50 Since it is stored along the screw plate 36 is configured to prevent the damage of the coal briquettes (50).

In order to prevent combustion of the coal briquettes 50 stored in the storage 35, the nitrogen of the nitrogen tank 34 is formed to flow into the storage tank 35.

Example

The present invention is to recycle the conventional farm waste to use as clean energy.

Palm waste used in the embodiment of the present invention includes palm fruit, palm stem, palm leaves and the like.

The farm waste 100 is placed in a crusher 13.

The palm waste 100 is crushed at the pitch interval of the blade 41 is formed spirally in the shredder (13).

The pitch of the shredder 13 is configured at intervals of 80 ~ 100mm.

The pitch of the shredder 13 as described above is 80 to 100mm because the cutting size of the farm waste 100 is cut to 80 to 100mm.

As described above, the farm waste 100 that has passed through the crusher 13 is transferred to the crusher 14a in a quantitative manner.

The crusher 13 is integrally formed with a fixed-quantity feeder 15a so that the crushed farm waste 100 is quantitatively supplied to the crusher 14a.

Palm waste 100 introduced into the grinder 14a is ground to a size of 30 ~ 60mm.

The crushed farm waste 100 is fed to the dryer 12 in a quantitative manner.

The dryer 12 is formed in a cylindrical shape and rotated as shown in Figure 3, and consists of an inner cylinder 61 and an outer cylinder 60, the crushed palm waste 100 is the dryer 12 Flows into the inner cylinder (61).

The palm waste 100 flowing into the inner cylinder 61 passes through the inner cylinder 61 and a part of the palm waste 100 moving to the hole 62 formed intermittently in the inner cylinder 61 flows out into the outer cylinder 60. do.

Since the inner cylinder 61 and the outer cylinder 60 are integrally formed, a part of the palm waste 100 leaked from the inner cylinder 61 is moved in the same direction as the palm waste 100 of the inner cylinder 61.

The dryer 12 is configured to form a slope of 3 to 6 degrees in the direction in which the farm waste 100 moves to adjust the moving speed of the farm waste 100.

Hot air of high temperature (150-350 ° C.) is introduced and circulated between the inner cylinder 61 and the outer cylinder 60 of the dryer 12 to dry the farm waste 100.

In addition, the incoming hot air is circulated while passing through the cyclone (25a), the gas separated from the dust and moisture is introduced into the combustor (23a) is configured to increase the thermal power of combustion.

As described above, the dryer 12 includes an inner cylinder 61 and an outer cylinder 60, and the farm waste 100 constitutes drying while passing through the inner cylinder 61 and the outer cylinder 60. When calculated by the tube is a length corresponding to twice the length of the dryer 12 of the present invention is configured to be able to perform a double amount of drying with a short length of the dryer.

Such a configuration becomes a configuration for drying the farm waste 100 at a water content of 20%.

The farm waste 100 dried as described above is supplied in a fixed quantity and is transferred to the carbonization furnace 11.

The carbonization furnace 11 has a structure in which the holes 72 are formed in the inner cylinder 71, the outer cylinder 70, and the inner cylinder in the same manner as the dryer 12.

However, the carbonization furnace 11 is configured horizontally, and the combustion gas jacket 27 through which high temperature (850 to 1000 ° C.) hot air is introduced and circulated is formed at the outer circumference of the outer cylinder 70. ) Will heat up.

The hot air circulating in the combustion gas jacket 27 as described above is configured to provide heat of 250 to 450 ° C. capable of carbonizing the farm waste 100 in the interior of the outer cylinder 70 and the interior of the inner cylinder 71.

Providing indirect heat to the carbonization furnace 11 as described above is for carbonizing the farm waste 100 in an intact state.

That is, when heat directly contacts the carbide 101, the carbide 101 may be burned to ash.

In addition, the scraper 29 is formed at any point of the outer periphery of the outer cylinder 70 so that the heat of the hot air circulating by removing the slag generated by the hot wind can be easily conducted into the outer cylinder 70.

As described above, the gas circulating in the combustion gas jacket 27 passes through the cyclone 25b, and tar and dust generated while carbonizing the palm waste 100 are separated and stored for use as a moisture and tar binder. Combustion gas of high temperature (400-450 degreeC) is comprised so that it may be used for circulation to the combustor 23b.

Carbide 101 of the carbonized palm waste is quantitatively transferred to the cooler 16a as described above.

Since the carbide 101 transferred to the cooler 16a is composed of a high temperature (400-450 ° C.), the carbide 101 is composed of a low temperature (80 ° C.) in order to mix the high temperature carbide 101 with a binder.

As described above, in order to gradually cool the high temperature carbide 101 to the low temperature carbide 101, it is configured to cool in three stages.

The carbide 101 of 400 ~ 450 ℃ in the first step is configured to cool to 200 ~ 250 ℃ in the second step and 80 ℃ or less in the third step.

In order to cool the coolers 16a, 16b, and 16c, a coolant jacket 28 is formed at the outer circumference of the coolers 16a, 16b, and 16c.

The coolant jacket 28 is configured to cool the coolers 16a, 16b, 16c while circulating the coolant in the coolant tower 26.

As described above, the cooling of the coolers 16a, 16b, and 16c by an indirect method is applied to the entire state of the carbide 101 in the same state in which the cooling temperature is applied to cool the time difference so that a part of the carbide 101 is of low quality carbide. It is for preventing that it is formed from 101.

As described above, while the high temperature (400-450 ° C.) carbide 101 passes through the first stage cooler 16a, the second stage cooler 16b, and the third stage cooler 16c, the carbide 101 may be 80 ° C. or less. The carbide 101 is constituted.

As the temperature of the carbide 101 is a high temperature (200-250 ° C.) until the high temperature carbide 101 is cooled as described above, the carbide 101 may be burned by ignition, so that nitrogen gas, which is an inert gas, may be arbitrarily selected. It is configured to prevent ignition while the carbide 101 is cooled to a low temperature (below 80 ° C.) by injection to form an intact carbide 101.

When the carbide 101 is cooled as described above, the carbide 101 is transferred to the grinder 14b using the screw conveyor 22a.

The conveyed carbide 101 is crushed to a thickness of 100 ~ 150 mesh is conveyed to the mixer 17.

The carbide 101 powder transferred to the mixer 17 is mixed with the binder in the binder reservoir 33.

When the carbide powder is mixed with the binder, tar generated in the carbonization furnace 11 is mixed together.

Carbide 102 mixed with the binder is quantitatively transferred to the molding machine 18.

As shown in FIG. 5, the molding machine 18 is configured such that the mixed carbide 102 that is introduced while the two rotating shafts of the molding machine 18 are engaged with each other and rotates is formed.

As described above, the mixed carbide 102 passing through the molding tool 51 of the molding machine 18 is molded to form the shape of the coal briquettes 50, and is formed with the mixed carbide 102 that is not molded. It breaks down into powder.

As described above, the mixed carbide 102 and the coal briquettes 50 that have passed through the molding machine 18 are transferred to the separator 19 so that the coal briquettes 50 are transferred to the coal briquettes 35 and are not formed. The mixed carbide 102 is again transferred to the mixer 17 and mixed with the binder.

The shaping coal 50 formed as described above is stored in the shaping coal 50 reservoir 35, and the reservoir 35 is freely injected with an inert gas to prevent the coal briquettes 50 from being ignited in the reservoir 35. To stabilize.

11: carbonization furnace 12: dryer
13 crusher 14 crusher (a, b)
15: fixed-quantity feeder (a, b, c) 16: cooler (a, b, c)
17 Mixer 18 Molding Machine 19 Separator 21 Conveyor 22 Screw Conveyor (a, b, c) 23 Combustor (a, b) 24 Condenser (a, b) 25 Cyclone (a, b) 26 Cooling Water Top 27: combustion gas jacket 28: cooling water jacket (a, b, c) 29: spiral cutter 31: dryer screw (a, b) 32: carbide screw (a, b) 33: binder storage 34: nitrogen gas tank 35 : Coal pool 36: Screw plate

Claims (14)

A crusher for crushing the farm waste, a pulverizer for crushing the crushed farm waste, a metering feeder composed of a screw to supply the crushed farm waste in a quantitative manner, and a combustor for drying the pulverized farm waste supplied in a quantitative manner. And a combustor configured to provide heat of 850-1000 ° C. for carbonizing the farm waste supplied at a high temperature of 400-450 ° C. And a binder mixed with a carbonized furnace which is heated by indirect heat at a high temperature of 850 to 1000 ° C., a cooler which is cooled by multiple stages of carbide carbonized by a high temperature of 400 to 450 ° C., and cooled by indirect heat, and a binder to the cooled carbide. And a fixed quantity feeder configured to supply mixed mixed carbides in a fixed quantity, and the mixed carbide supplied in a fixed quantity. Apparatus for manufacturing a molding with a carbon farm waste, characterized in that consisting of a molding machine and, as a separator for separating the formed carbon and mixed carbides formed in the molding machine, a reservoir for storing the carbon for forming. The apparatus of claim 1, wherein the blade of the shredder is formed to protrude spirally on the rotation axis of the shredder and the pitch of the blade is equal to the size of the farm waste to be shredded. 2. The dryer of claim 1, wherein the dryer is configured to rotate and consist of an outer cylinder and an inner cylinder, and a screw is formed inside the inner cylinder and the outer cylinder so as to move the farm waste, and an inner cylinder is formed intermittently with a hole over its length. Palm waste moving the outer cylinder is configured to discharge while moving from the inner cylinder to the outer cylinder from the inner cylinder to the inner cylinder through the hole, characterized in that for producing the coal briquettes using the palm waste. According to claim 1, wherein the carbonization furnace is composed of the outer cylinder and the inner cylinder is configured to rotate, the inner cylinder and the inside of the outer cylinder is formed to move the carbonized palm waste is formed and the inner cylinder is formed intermittently over the length thereof Palm waste moving the inner cylinder and the outer cylinder is discharged while moving from the inner cylinder to the outer cylinder from the outer cylinder to the inner cylinder through the hole, and a combustion gas jacket is formed to allow the combustion gas to circulate on the outer periphery of the outer cylinder. Apparatus for producing coal briquettes using palm waste, characterized in that configured to provide indirect heat. The method of claim 4, wherein a scraper is formed outside the outer cylinder of the carbonization furnace to remove slag generated by the combustion gas circulated in the combustion gas jacket of the outer cylinder to facilitate heat conduction inside the carbonization furnace. An apparatus for producing coal briquettes using a farm waste, characterized in that: 2. The farm waste of claim 1, wherein a coolant jacket is formed outside the cooler such that the coolant in the tower circulates through the coolant jacket and indirectly provides cooling heat to the cooler to indirectly cool the hot carbide. Apparatus for manufacturing molded coal using a. 7. The apparatus of claim 6, wherein an inert gas is optionally injected into the cooler to prevent ignition of the cooled high temperature carbide. The apparatus of claim 1, wherein the carbide powder mixed in the mixer is configured to mix the binder and water to form the coal briquettes. The method of claim 1, wherein the molded coal and the non-molded mixed carbide is passed through the molding machine in the separator, the coal is stored in the storage and moved to the storage, and the mixed carbide that is not formed is transferred to the mixer and mixed again with the binder. Apparatus for producing coal briquettes using farm waste. According to claim 1, wherein the storage tank is stored in the form of a screw plate-shaped slope is formed so that the formed coal is stored using the slope is configured to prevent the destruction of the coal briquettes during storage of the coal briquettes Apparatus for producing coal briquettes using the farm waste, characterized in that. 12. The apparatus of claim 10, wherein the injecting gas is injected into a reservoir in which the coal briquettes are stored to prevent the coal briquettes from igniting. The apparatus of claim 3, wherein the residual heat of the drying heat circulating through the dryer is purified while passing through a cyclone, moisture and dry gas are separated, and the separated gas is introduced into a combustor. [5] The coal briquettes of claim 4, wherein dust, tar, and moisture generated by carbonization in a carbonization furnace pass through a cyclone, and dust is separated and stored for use as a binder. Manufacturing equipment. 5. The apparatus for producing coal briquettes using palm waste according to claim 4, wherein the high temperature combustion gas circulating through the combustion gas jacket of the carbonization furnace is circulated to the combustor of the carbonization furnace.

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