JP2006082042A - Organic waste drying system - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To uniformly dry the waste of foods such as vegetables containing much water to drying in a short period of time. <P>SOLUTION: The organic waste drying system is provided with: a pulverizing device 3 of pulverizing organic waste largely containing water, so as to be slurry; a storing device 4 of storing the slurry pulverized by the pulverizing device 3; a pump carrying device 5 of quantitatively carrying the slurry stored in the storing device; and a drying device 6 of drying the slurry carried by the pump carrying device 5, and, in the drying device, moisture comprised in the slurry is evaporated, and a solid component is dried to a prescribed dryness. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

  The present invention relates to an organic waste drying system for drying organic wastes containing a large amount of moisture such as bean sprouts, radish, cabbage and other waste vegetables and waste flowers.

As a conventional organic waste drying system, for example, a container for storing a paste-like or low-viscosity treatment product or sludge, a gas supply means for supplying a dry gas into the container, and a vertical arrangement in the container are provided. An agitator comprising stirring blades that can be rotated around a vertical axis, and a chopper that is disposed on a side surface of the container and that can rotate about a horizontal axis perpendicular to the central axis while stirring the processed material There has been proposed a vertical stirring and drying device that is dried with a dry gas and exhausts the dried processed product together with an exhaust gas from an exhaust port at the top of the container (see, for example, Patent Document 1).
JP-A-7-202655 (first page, FIG. 1)

However, in the conventional example described in Patent Document 1, bean sprouts generated in bean sprouts manufacturing plant, mixed vegetable manufacturing plant, etc., when waste of vegetables with high water content such as radish, cabbage, etc. is input as it is. Although there is an agitator and a chopper, there is an unsolved problem that the crushing cannot be performed sufficiently finely in a short time, and the drying treatment time becomes long.
Therefore, the present invention has been made paying attention to the unsolved problems of the above-mentioned conventional example, organic waste drying that can uniformly dry food waste such as vegetables with a high content of moisture in a short time It also aims to provide a system.

In order to achieve the above object, the organic waste drying system according to claim 1 is an organic waste drying system in which the first technical means dries organic waste containing a large amount of moisture,
A pulverizing device that pulverizes the organic waste into a slurry, a storage device that stores the slurry pulverized by the pulverizing device, a pump transfer device that quantitatively conveys the slurry stored in the storage device, and the pump transfer device And a drying device that dries the slurry conveyed in (1).
Further, in the organic waste drying system according to claim 2, in the invention according to claim 1, the pulverizing apparatus is configured to continuously input the organic waste from the quantitative charging means and the quantitative charging means for quantitatively charging the organic waste. And crushing means for crushing.

  Furthermore, the organic waste drying system according to claim 3 is the invention according to claim 2, wherein the pulverizing means is rotatable into a cylindrical container into which the organic waste is charged from the fixed amount charging means, and into the cylindrical container. A predetermined number of cutting blades attached to a central shaft disposed on the inner peripheral surface of the cylindrical container and extending in an axial direction disposed at predetermined intervals in the circumferential direction on the outer peripheral end of the cutting blade. A baffle plate that is opposed to the cutting blade of the cylindrical container, a discharge port having a large number of through holes provided at a position facing the cutting blade of the cylindrical container, and a rotational drive mechanism that rotationally drives the central axis. It is characterized by having.

Furthermore, the organic waste drying system according to claim 4 is the invention according to claim 3, wherein the cylindrical container restricts an input area of the organic waste with respect to the cutting blade to the input port of the organic waste. It is characterized in that a charging guide plate for guiding is formed.
Still further, the organic waste drying system according to claim 5 is the invention according to any one of claims 1 to 4, wherein the drying device includes a heating chamber having a heating source formed on a gantry, and the heating chamber. A drying kettle having a bottom portion that is shaped like an inverted frustoconical shape and receives a slurry that is continuously metered in by the pump conveying device disposed in the base, and has a discharge port on the bottom side; and the drying kettle And a transport drying means for performing secondary drying while transporting the dried food discharged from the container.

Moreover, the organic waste drying system according to claim 6 is the invention according to claim 5, wherein the drying device includes secondary combustion means for secondary combustion of exhaust gas exhausted from the drying pot and the transport drying means. It is characterized by having.
Furthermore, the organic waste drying system which concerns on Claim 7 is provided with the crushing blade which has a vertical blade part along the reverse frustoconical internal peripheral surface in the invention which concerns on Claim 5 in which the said drying pot rotates inside. It is characterized by having.
Furthermore, the organic waste drying system according to claim 8 is the invention according to any one of claims 5 to 7, wherein the transfer drying means is introduced with a heating gas in the heating chamber as a heating gas. It is characterized by.

According to the first aspect of the present invention, organic waste containing a large amount of water is pulverized by a pulverizer to form a slurry, which is stored in a storage device and then separated into a drying device by a pump conveyance device without solid-liquid separation. Since direct quantitative conveyance is performed, the slurry can be efficiently and quickly dried with a drying apparatus, and the effect that the drying processing time can be greatly shortened can be obtained.
According to the invention of claim 2, since the organic waste is quantitatively charged into the pulverizing means by the quantitative charging means, a constant pulverization efficiency can be secured by the pulverizing means, and the solid matter contained in the slurry is pulverized. The effect that the shapes can be aligned is obtained.

  Further, according to the invention of claim 3, the pulverizing means is a cylindrical container into which the organic waste is introduced from the fixed quantity introducing means, and a predetermined shaft attached to a central shaft rotatably disposed in the cylindrical container. A number of cutting blades, a baffle plate extending in the axial direction disposed at a predetermined interval in the circumferential direction on the inner peripheral surface of the cylindrical container, and facing the outer peripheral end of the cutting blade at a slight distance; Since it has a discharge port with a large number of through holes arranged at positions facing the cutting blade of the cylindrical container and a rotation drive mechanism that rotationally drives the central axis, it is located between the cutting blade and the baffle plate. The organic waste is pulverized and made into a slurry, and the slurry is discharged through the through-holes, so that the shape of the solid matter contained in the discharged slurry can be surely made uniform. It is done.

  Furthermore, according to the invention according to claim 4, since the introduction guide plate for guiding the organic waste while restricting the input area of the organic waste to the cutting blade is formed in the cylindrical container, Even when the bulk density when organic waste is pulverized increases several times to several tens of times, it is possible to perform good crushing processing by suppressing slurry overflow in the crushing chamber containing the cutting blade. The effect is obtained.

Still further, according to the invention according to claim 5, since the slurry is primarily dried in the drying kettle and then secondarily dried by the transport drying means, the effect that the degree of drying of the organic waste can be accurately controlled. Is obtained.
According to the invention of claim 6, since the exhaust gas exhausted from the drying kettle and the transport drying means is subjected to secondary combustion by the secondary combustion means, the generation of dioxins is reliably prevented, and the clean exhaust gas is discharged into the atmosphere. The effect that it can be released is obtained.

Furthermore, according to the invention which concerns on Claim 7, since the drying pot is equipped with the crushing blade which has a vertical blade part along the inner peripheral surface of the inverted truncated cone rotated inside, it is thrown in by this crushing blade. The effect that the drying process time can be shortened by effectively convectioning the slurry is obtained.
Furthermore, according to the invention according to claim 8, since the heating gas of the heating chamber is introduced as the heating gas in the transport drying means, it is not necessary to provide a separate heating source, and the exhaust heat of the heating chamber is efficiently obtained. The effect of being able to use well is acquired.

Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a system configuration diagram showing an embodiment in which the present invention is applied to an organic waste drying system for drying waste bean sprouts generated in a bean sprouts manufacturing plant. In the figure, 1 is an organic waste drying system. The organic waste drying system 1 includes a solid-water separator 2 that recovers by washing away sprouts of sprouts produced at a bean sprout manufacturing plant and sprouts that fall on the floor with water, and this solid-water separator. A pulverizer 3 for pulverizing waste bean sprouts separated from water by the machine 2, a storage tank 4 as a storage device for storing the slurry discharged from the pulverizer 3, and the tank 4. A pump transport mechanism 5 serving as a pump transport device for supplying a fixed amount of slurry and a drying device 6 for drying the slurry transported by the pump transport mechanism 5 are configured.

The pulverizing apparatus 3 was transported by a hopper 31 into which sprouts separated from the water supplied from the solid water separator 2 were thrown in, a conveyor 32 with a bar that cuts out sprouts from the lower end of the hopper 31, and a conveyor 32 with the bar. A shredder 33 is provided as pulverizing means for pulverizing with bean sprouts.
As shown in FIGS. 2 and 3, the shredder 33 has a cylindrical container 34 whose upper end is widened in a funnel shape. The bean sprouts that are formed and fed from the charging port 35 are sent to the crushing chamber 36 formed in the middle stage, and are crushed in the crushing chamber 36 and the slurry is discharged from the discharge port 37.

  The crushing chamber 36 includes a central shaft 36c rotatably disposed on support plates 36a and 36b fixed to a substantially central position and a lower position in the vertical direction of the cylindrical container 34, and a three-stage mounted on the central shaft 36c. Cutting blades 36d, a plurality of baffle plates 36e extending axially at predetermined intervals in the circumferential direction on the inner peripheral surface of the cylindrical container 34 facing the outer peripheral ends of the cutting blades 36d at a slight distance, and the cylindrical container A discharge port 36f formed of punch metal having a large number of through holes with a predetermined diameter mounted between predetermined predetermined baffle plates 36e, and a discharge chute 36g extending obliquely downward from the outside of the discharge port 36f. A drive motor 36h that rotationally drives a central shaft 36c disposed outside the cylindrical container 34, a pulley attached to the rotational shaft of the drive motor 36h, and a pulley attached to the central shaft 36c. It is composed of a belt 36i.

  Here, as shown in FIG. 3, the cutting blade 36d has a configuration in which two strip-shaped blade portions are combined in a cross shape, and its outer peripheral edge is directed upward toward the baffle plate 36e in the upper two steps. The upper inclined end portion 36j is formed to extend, and one end portion of each blade portion is formed at the upper inclined end portion 36k for the remaining lower one step, and the other end portion is lowered downward toward the baffle plate 36e. It is formed at the extending lower inclined end. In this way, the cutting blade 36d is formed in three stages, and the upper inclined end portion 36j and the lower inclined end portion 36k are formed on the outer peripheral end thereof, so that the cutting blade 36d is made between the upper inclined end portion 36j and the baffle plate 36e. The solid bean sprouts that are crushed into a predetermined shape that can pass through the diameter of the discharge port 36f while crushing the palm between the lower inclined end and the baffle plate 36e. It is composed of water and moisture, and the slurry can be pushed out to the discharge port 36f.

The storage tank 4 has a stirring blade 43 that is attached to a rotating shaft of an electric motor 42 fixed to the upper lid 41 and extends into the tank. By rotating the stirring blade 43, the stored slurry is separated into solid and liquid. The discharge port 44 provided in the lower part is communicated with the pump conveyance mechanism 5.
The pump transfer mechanism 5 includes a positive displacement transfer pump 51 called a so-called sine motor having a sine curve-shaped rotor whose rotation speed is controlled, one end communicating with the discharge port 43 of the storage tank 4, and the other end Is connected to the suction side of the transfer pump 51, one end is connected to the discharge side of the transfer pump 51, and the other end extends upward and is connected to the upper part of the drying pot 62 of the drying device 6. The slurry in the storage tank 4 is quantitatively supplied every predetermined time.

The drying device 6 includes a heating chamber 63 having a combustion burner 62 as a heating source formed on a pedestal 61, a drying pot 64 disposed in the heating chamber 63, and a discharge port 64 a of the drying pot 64. An upper transport mechanism 65 for transporting the primary dried pulverized bean sprout upward, a transport drying mechanism 66 for performing secondary drying while transporting the pulverized sprouts transported by the upper transport mechanism 65, a drying pot 64, and transport drying And a secondary combustion mechanism 67 for sucking dry gas in the mechanism 66 and performing secondary combustion.
Here, the drying pot 64 is composed of an upper cylindrical portion 64b and an inverted truncated cone-shaped conical cylinder portion 64c that is formed in a funnel shape and communicates with the cylindrical portion 64. A crushing blade 64e is attached to a rotating shaft 64d that is rotatably disposed at a position eccentric from the shaft.

  As shown in FIGS. 4 to 6, the crushing blade 64e extends radially from the outer peripheral surface of the cylindrical mounting boss portion 64f at equal intervals in the circumferential direction, and crushes at a predetermined angle θ with respect to the horizontal plane. It has a body 64g. One set of crushed bodies 64g opposed to each other with the mounting boss 64f interposed therebetween is composed of a base portion 64h and an extension portion 64i extending from the base portion 64h along the inner peripheral surface of the conical head portion 64c. A blade portion 64j that crushes when rotating clockwise is formed. The other set of crushed bodies 64g is composed of only a base portion 64h, and a blade portion 64k that crushes when rotating counterclockwise is formed at the upper end of the base portion 64h. In this crushing, 64e is rotationally driven by the attachment boss portion 64f being connected to the rotation shaft of the drive motor 64l disposed on the lower surface of the mount 61.

  And the discharge port 64a is formed in the side wall by the side of the right end side where the base 64h of the crushing body 64g in the crushing blade 64e of the drying pot 64 adjoins, and this discharge port 64a is provided with this discharge port 64a as shown in FIG. A first opening / closing door 64m that opens and closes is disposed, and the opening / closing door 64m is opened and closed by an actuator 64n. A discharge chute 64o that covers the open / close door 64m and opens to the lower end of the heating chamber 63 is disposed at the discharge port 64a, and a second open / close door 64p that opens and closes the open chute 64o is disposed at the open end of the discharge chute 64o. The opening / closing door 64p is opened / closed by an actuator 64q. Further, a discharge chute 64r extending downward is provided so as to cover the open / close door 64q. Furthermore, a semicircular inlet 64s for receiving the slurry conveyed by the conveying pipe 53 of the upper conveying mechanism 5 is formed at the upper end of the cylindrical portion 64b, and a damper valve 64t is provided in the inlet 64s. The damper valve 64t is driven to open and close by the actuator 64u. An exhaust pipe 64v is connected in front of the input port 64s.

  Further, the upper transport mechanism 65 has a bucket conveyor 65a that moves horizontally from the introduction port disposed opposite to the open end of the lower end of the discharge chute 64r, then moves vertically, and moves horizontally from the upper end. The primary combusted waste bean sprouts discharged from the discharge chute 64r by the bucket conveyor 65a are conveyed upward and transferred from the upper discharge chute 65b to the secondary combustion mechanism 66.

  Further, as shown in FIGS. 1 and 7, the transport drying mechanism 66 includes a screw conveyor 66 a that receives the waste bean sprouts that are primarily burned from the discharge chute 65 b of the bucket conveyor 65 a of the upper transport mechanism 65, and this screw conveyor 66 a A heating cylinder 66c to which heated gas from the heating chamber 63 is supplied via the communication pipe 66b is disposed on the outer periphery of the primary combustion chamber, and the primary burned waste bean sprouts conveyed by the screw conveyor 66a by the heating cylinder 66c are secondary. The fuel is burned and collected in the collection container 66e from the discharge port 66d at the rear end. Here, the water content of the finally dried bean sprouts is measured, and the rotation speed of the screw conveyor 66a, that is, the conveying speed of the waste bean sprouts is controlled so that the amount of the water becomes a set value.

  Furthermore, the secondary combustion mechanism 67 introduces exhaust gas exhausted from the waste pipe 64v of the drying pot 64 and the heating cylinder 66c of the transport drying mechanism 66 into the cylindrical secondary combustion chamber 67a. The secondary combustion burner 67b disposed in 67a causes secondary combustion at 800 ° C. or higher to prevent the generation of dioxins and the generation of odor, and is sucked into the chimney 67d by sucking negative pressure by the air supplied from the blower 67c. Discharged.

Next, the operation of the above embodiment will be described.
At this time, when the bean sprouts are sprinkled on the floor in the manufacturing process, the sprouts such as unsatisfied sprouts whose length does not meet the standards, and the sprouts that fall on the floor in the manufacturing process are washed out with water and transported to the solid water separator 2. The bean sprouts and water are separated by the machine 2 and only the bean sprouts are put into the hopper 31 of the crushing device 3.

  The bean sprouts thrown into the hopper 31 are cut out from the lower part by a cross conveyor 32 at a substantially constant amount and put into the shredder 33. When waste bean sprouts are put into the shredder 33, it is crushed by, for example, a cutting blade 36d rotated at 3000 revolutions per minute. At this time, both ends of the upper two-stage cutting blade 36d are formed at the upper inclined end portion 36j, one end of the remaining lower one-stage cutting blade 36d is formed at the upper inclined end portion 36j, and the other end is the lower inclined end portion. Since the upper beveled edge 36j and the baffle plate 35e cooperate with each other to form a convection by pulverizing the waste bean sprout upwardly, and sufficiently pulverizing the solid content of the bean sprout When the slurry mixed with moisture is formed, it is pushed out to the discharge port 35f made of punching metal by the lower inclined end portion 36k, passes through the through-hole, passes through the discharge chute 36g, and is put into the storage tank 4. The Here, when the shape of the solid portion contained in the slurry is changed, the discharge port 35f may be changed to punch metal having a different diameter of the through hole.

In the storage tank 4, the charged slurry is constantly stirred by the stirring blade 43 so that solid-liquid separation does not occur, and the stirred slurry is supplied to the drying device 6 by the pump transport mechanism 5.
At this time, the transport pump 51 of the pump transport mechanism 5 is relatively gradual so that a sudden temperature drop does not occur in the drying pot 64 due to the slurry having a temperature close to the outside temperature when the slurry is charged into the drying pot 64 of the drying device 6. When the slurry is supplied and the charging of a predetermined amount, for example, 10 kg of slurry to the drying pot 64 is completed, the damper valve 64t formed at the charging port 64s is closed by the actuator 64u, and in this state or before, the drive motor 64l is turned on. The cutting blade 64e is rotationally driven by being rotationally driven. Since the cutting blade 64e is eccentric with respect to the drying pot 64, a narrow space and a wide space are formed between the conical cylinder portion 64c of the drying pot 64 and the tip of the cutting blade 64e. When the solid content in the mixed slurry moves toward a narrow gap, it is crushed between the cutting blade 64e and the inner peripheral surface of the conical cylinder portion 64c serving as a heat transfer surface, and a crushing action is exerted.

  At this time, since the drying pot 64 is disposed in the heating chamber 63, it is heated by the heated gas in the heating chamber 63, so that the moisture of the charged slurry is evaporated and exhausted from the exhaust pipe 64 v, and the remaining The primary drying is performed, for example, for 5 minutes until the weight of the solid content decreases from about 10 kg to about 2 kg. When the drying time elapses, the first opening / closing door 64m is first opened by the actuator 64n while the crushing blade 64e is rotated, and the cone The primary dried waste bean sprouts in the cylinder part 64c are discharged into the discharge chute 64o.

  Then, when a sufficient time has elapsed for all of the primary dried waste bean sprouts in the conical cylinder portion 64c to be discharged into the discharge chute 64o, the first opening / closing door 64m is closed by the actuator 64n. When 64m is completely closed, the actuator 64u opens the damper valve 64t of the input port 64s, the conveyance by the conveyance pump 51 of the pump conveyance mechanism 5 is started, and the second opening / closing door 64p is opened by the actuator 64q. The primary dried waste bean sprouts in the discharge chute 64o are transferred to the bucket conveyor 66a of the upper transfer mechanism 65 through the discharge chute 64r, and are transferred upward by a certain amount and received by the screw conveyor 66a of the transfer drying mechanism 66. Passed.

In the transport drying mechanism 66, a heating cylinder 66c to which the heated gas from the heating chamber 63 is supplied is provided around the screw conveyor 66a. Therefore, the primary transported by the screw conveyor 66a by the radiant heat from the heating cylinder 66c. The dried bean sprouts are secondarily dried and dried to an extent that can be handled as garbage having a desired degree of dryness, for example, about 300 g in weight, and the secondly dried bean sprouts are collected in the collection container 66e. .
At this time, the dryness of the waste sprouts collected in the recovery container 66e is monitored continuously or batchwise, and the rotational speed of the screw conveyor 66a is controlled so that the dryness of the waste sprouts becomes an appropriate value.

  Thus, according to the above-described embodiment, the bean sprouts discarded from the bean sprouts manufacturing plant are pulverized by the pulverizer 3 and stored in the storage tank 4 as a slurry in which solid content and moisture are mixed, and stored in this storage tank 4. Since the slurry is transported to the drying device 6 by the pump transport mechanism 5, since the solid content contained in the slurry charged to the drying device 6 is subdivided, the waste bean sprouts are directly input to the drying device 6. Compared to the case, the drying time can be greatly shortened.

  Moreover, the waste bean sprouts are crushed by the crushing device 6 and become a slurry in which the solid content and moisture are mixed, and the slurry is supplied to the drying device 6 by the pump transport mechanism 5 without separating the solid water, so that the drying device 6 Can be accurately controlled, and can be introduced while suppressing an increase in the volume of moisture due to a temperature difference at the time when the slurry is introduced into the drying pot 64 of the drying device 6. It can be carried out.

  Furthermore, since the drying device 6 performs primary drying with the drying pot 64 and the transport drying mechanism 66 performs secondary drying, the drying process time is shortened by the primary drying with the drying pot 64, and the transport drying mechanism 66 continues to dispose of the waste. It is possible to accurately control the dryness of the bean sprouts, to ensure that the amount of moisture in the waste bean sprouts becomes too low and carbonized to be treated as industrial waste and to be treated to an appropriate dryness. it can.

In the above embodiment, the case where the bean sprouts are applied as the organic waste has been described. However, the present invention is not limited to this, and the disposal of radishes, cabbages, tomatoes and the like with a high content of water to be discarded in the vegetable processing factory is not limited thereto. In addition to being able to apply the present invention to vegetables, the present invention can also be applied to other organic waste such as seaweed and cut flowers. When slurry cannot be formed, water may be separately supplied and stored in the storage tank 4 as slurry.
Moreover, in the said embodiment, although the case where a slurry was supplied to the one drying apparatus 6 via the one pump conveyance mechanism 5 to the storage tank 4 was demonstrated, it is not limited to this, A storage tank The slurry may be transported from 4 to a plurality of drying devices 6 via a plurality of pump transport mechanisms 4, and drying processing may be performed in parallel by each drying device 6.

  Furthermore, in the above-described embodiment, the example of the present invention is merely shown. The crushing device 3 is not limited to the configuration of the above-described embodiment, and the slurry is pulverized to such an extent that the organic waste after drying is not carbonized. Any pulverizing apparatus can be applied as long as it can be converted into a pulverizing apparatus. Similarly, the drying device 6 is not limited to the configuration of the above-described embodiment, as long as the slurry can be charged to evaporate moisture and dry the remaining solid content to an appropriate degree of dryness. A drying device can be applied, and in this case, the drying device is not limited to the case of performing the drying twice of primary drying and secondary drying, and a drying device including any number of drying steps can be applied.

It is a schematic structure figure showing one embodiment of the present invention. It is the side view which made the cross section the part which shows the shredder of the crushing apparatus. FIG. 3 is a plan view of FIG. 2. It is a top view which shows the crushing blade of a drying pot. It is a front view which shows the crushing blade of a drying pot. It is a side view which shows the crushing blade of a drying pot. It is a side view which shows a conveyance drying mechanism.

Explanation of symbols

  DESCRIPTION OF SYMBOLS 1 ... Organic waste drying system, 2 ... Solid water separator, 3 ... Crushing device, 31 ... Hopper, 32 ... Conveyor with a cross, 33 ... Shredder, 36e ... Baffle plate, 36d ... Cutting blade, 36h ... Drive motor, 4 ... Storage tank, 42 ... drive motor, 43 ... stirring blade, 5 ... pump transfer mechanism, 51 ... transfer pump, 52, 53 ... transfer pipe, 6 ... drying device, 61 ... mount, 62 ... combustion burner, 63 ... heating chamber, 64 ... Drying pot, 64e ... Crushing blade, 65 ... Upper transfer mechanism, 66 ... Transfer drying mechanism, 66a ... Screw conveyor, 66c ... Heating cylinder

Claims (8)

An organic waste drying system for drying organic waste containing a large amount of moisture,
A pulverizing device that pulverizes the organic waste into a slurry, a storage device that stores the slurry pulverized by the pulverizing device, a pump transfer device that quantitatively conveys the slurry stored in the storage device, and the pump transfer device An organic waste drying system, comprising: a drying device that dries the slurry conveyed in (1).   2. The pulverizing apparatus includes: a quantitative charging unit configured to quantitatively input organic waste; and a pulverizing unit configured to continuously pulverize the organic waste from the quantitative charging unit. Organic waste drying system.   The pulverizing means includes a cylindrical container into which the organic waste is introduced from the quantitative charging means, a predetermined number of cutting blades attached to a central shaft rotatably disposed in the cylindrical container, A baffle plate extending in the axial direction disposed at a predetermined interval in the circumferential direction on the inner peripheral surface and facing the outer peripheral end of the cutting blade at a slight distance, and a position facing the cutting blade of the cylindrical container The organic waste drying system according to claim 2, further comprising: a discharge port provided with a plurality of through-holes disposed in the shaft, and a rotation driving mechanism that rotationally drives the central shaft.   4. The organic waste according to claim 3, wherein the cylindrical container is formed with an introduction guide plate that guides the organic waste while restricting an input area of the organic waste with respect to the cutting blade. Product drying system.   The drying device has a heating chamber having a heating source formed on a gantry, and a bottom portion for receiving primary slurry and receiving primary slurry by continuously receiving a fixed amount of slurry by the pump transfer device disposed in the heating chamber. A drying kettle having a trapezoidal shape and having a discharge port on the bottom side thereof, and a transport drying means for secondary drying while transporting the dried food discharged from the drying kettle. 5. The organic waste drying system according to any one of 1 to 4.   The organic waste drying system according to claim 5, wherein the drying device includes secondary combustion means for secondary combustion of exhaust gas exhausted from the drying pot and the transport drying means.   The organic waste drying system according to claim 5, wherein the drying pot includes a crushing blade having a vertical blade portion along an inner peripheral surface of an inverted truncated cone that is rotationally driven inside.   The organic waste drying system according to any one of claims 5 to 7, wherein a heating gas in the heating chamber is introduced into the transport drying means as a heating gas.

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