JP3106116B2 - Granulator - Google Patents

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a granulating apparatus for sludge-like substances or powdery substances which have been dehydrated into cakes, and more particularly to the prevention of environmental pollution due to the scattering of products and the portability of the products. The present invention relates to a granulating apparatus for improving the quality and the like.

[0002]

2. Description of the Related Art A technique for adding lime to a sludge-like substance to reduce the water content and thereby granulating the sludge-like substance is as follows.
JP-B-54-121330 and JP-B-7
-98200.

[0003] In this case, in many cases, dewatered sludge-like substances (hereinafter referred to as "cake") are made into granules or granules to improve portability, or to enhance the durability during long-term storage and effectively reduce environmental pollution due to scattering. It is intended to prevent this.

For example, lime is put into a cake obtained by dewatering sewage sludge (water content of about 96 to 98%) to about 80%, and is reacted with moisture. Has been conventionally used as a fertilizer.

FIG. 23 shows a conventional example of a tornado fin type as one of the sludge-like substance drying / granulating apparatuses. This figure 2
The drying / granulating apparatus of the tornado fin type shown in FIG. 3 is equipped with a heater 102 around a casing 101 for storing sludge, and a main shaft 103 disposed at the center thereof.
And a spiral tornado fin 10 integrated therewith
The lower part is provided with a sludge carry-in part 105 for feeding cake at one end, and a carry-out conveyor 106 for sending dry sludge at the other end.

In this case, the sludge in the casing 101 is
A strip-shaped rake member (the main shaft 103 and the tornado fins 104) arranged along the bottom plate portion in the casing 101.
Tornado fin 1
The sludge is conveyed upward along the spiral surface of the tornado fin 104 in combination with the centrifugal force applied to the sludge as the tornado fin 104 is rotated in the direction of arrow A. Is done. Then, it is heated by the heater 102 during the upward transfer process.

[0007] The granular sludge that has reached the upper part is swept to the center by the baffle plate 110. Hereinafter, by repeating this, the sludge is dried and granulated.
Here, reference numeral 112 denotes an evaporating water discharging section. Reference numeral 116 denotes a driving device for driving the tornado fin 104 to rotate.

[0008]

However, in each of the above-mentioned prior arts, kneading and granulation of the granulation target are performed relatively well, but sizing is not necessarily performed well. There is nothing. For this reason, for example, in the case of converting sludge treated in large quantities into fertilizer, if the particle size is extremely large, mechanical sowing cannot be performed when used as fertilizer, and at the same time the effect as fertilizer becomes slower. there were. On the other hand, if the particle size is too small, the particles are liable to be scattered by the wind, so that the commercial value is greatly reduced.

Further, in the conventional examples, there are many single-function devices that only include kneading, kneading and granulation, granulation only, granulation and sizing, or sizing alone. In particular, in the case of a sizing apparatus, many of them are themselves large. For this reason, when a system is constructed in which the kneading function, the granulating function, and the sizing function are sequentially connected in series, there is a disadvantage that the entire apparatus becomes large, occupies a large area, and becomes expensive.

[0010]

SUMMARY OF THE INVENTION The object of the present invention is to improve the disadvantages of the prior art, and particularly to sludge-like substances or powdery substances, etc., each of which has the functions of kneading, granulating and sizing, and the entire apparatus. It is an object of the present invention to provide a granulating device capable of miniaturization and multifunctionalization.

[0011]

In order to achieve the above object, according to the first aspect of the present invention, in the first aspect of the present invention, a substance carrying section for carrying in a predetermined amount of sludge-like substance which has been dehydrated and caked. , A spiral tornado fin rotatably arranged along the inner wall of the casing, and a tornado fin arranged at the center shaft portion of the casing for holding and rotating the tornado fin A main shaft, a plurality of kneading blades fixedly held to the main shaft, a fixed baffle plate mounted on the upper end portion of the casing and sweeping down the particulate matter rising along the spiral surface of the tornado fin described above, and a casing. A granulated material discharge unit that discharges the granulated sludge-like substance provided at a predetermined position on the side surface of the exhaust gas discharge unit that discharges exhaust gas in the casing, It is mounted in the pacing and a spindle drive means for rotating the spindle described above.

The sludge-like substance (granulation target) kneaded and partially granulated at a predetermined position on the spiral surface of the tornado fin is prevented from rolling upward in the spiral surface and is formed. In the graining stage, a configuration is adopted in which rolling control means for allowing rolling in the upward direction is provided.

Therefore, according to the first aspect of the present invention,
First, an appropriate amount of lime is added to the dehydrated cake to start the hydration reaction. Thereafter, when a predetermined time elapses and the water content becomes suitable for granulation, the spiral surface of the tornado fin during rotation is rolled. The movement restricting means is disengaged and becomes a rolling surface to promote granulation.

In this case, for example, when the water content of the sludge-like substance is high, the rolling restricting means is operated to substantially shorten the length of the spiral surface of the tornado fin, thereby preventing upward rolling. Thereby, the kneading is promoted, and at the same time, the operation of the rolling control means is stopped from the granulation stage to increase the length of the spiral surface of the tornado fin, thereby promoting the granulating and sizing functions. In addition, various operations can be performed according to the water content of the dewatered cake. Also, in this case, it is gradually adjusted to a predetermined diameter (for example, about 6 mm) and rises while rolling with the rotation of the tornado fin,
It is discharged from the discharge section as granulated granulated material.

According to a second aspect of the present invention, in the granulating apparatus of the first aspect, the rolling restricting means is constituted by a flapper mechanism formed by forming a part of the tornado fin so as to be able to move up and down. To do that.

For this reason, since a part of the tornado fin is cut out and formed to be able to pivot up and down, the tornado fin is substantially shortened to increase the effectiveness of the kneading operation, or to lengthen the granulation and crushing. It is possible to select and set a usage method according to the process such as making the sizing operation effective.

According to a third aspect of the present invention, in the granulating apparatus according to the second aspect, the flapper mechanism includes a bridging plate that forms a part of the tornado fin, a bridging plate that holds the bridging plate, and the bridging plate. The above-mentioned method is adopted in which the drive shaft is configured by a drive shaft that urges the up-and-down rotation in the direction along the surface of the tornado fin, and a shaft drive unit that urges the drive shaft to perform a predetermined operation. I have. Therefore, the versatility can be further improved in that the operation stop of the flapper mechanism can be easily selected and set from the outside.

According to a fourth aspect of the present invention, there is provided the granulating apparatus according to the first aspect, wherein the rolling restricting means is removably disposed at a predetermined position on the spiral surface of the tornado fin. A variable baffle plate mechanism having a plate is adopted.

For this reason, when the tornado fin is used short on the spiral surface, the movable baffle plate is arranged so as to cross the spiral surface, and when the tornado fin is used long on the spiral surface, By rotating the movable baffle plate and performing an operation of pulling it away from the helical surface, it is possible to obtain the same operation and effect as the above-described invention 2 without reworking the tornado fin,
Productivity and maintainability are improved.

According to a fifth aspect of the present invention, in the granulating apparatus of the fourth aspect, the variable baffle plate mechanism includes a movable baffle plate disposed at a predetermined position on a spiral surface of the tornado fin, A fixed arm having a baffle plate rotatably held inside the above-described tornado fin and having one end fixed to the main shaft, and the tornado described above being disposed substantially parallel to the fixed arm and reciprocating along a central axis. A drive arm for urging the fin to rotate and a cam mechanism for urging the drive arm with a driving force are provided, and the cam mechanism is provided in the main shaft described above.

Therefore, in the invention according to claim 5,
In addition to functioning equivalently to the above-described claim 4, the movable baffle plate can be disposed at a predetermined position on the spiral surface of the tornado fin by an external operation, and at this point, the movable baffle plate is always This is convenient because it can be arranged at an optimum position.

According to a sixth aspect of the present invention, in the first, second, third, fourth, or fifth aspect, at least one of the plurality of kneading blades is a perforated blade having a particle size regulating function. Is adopted.

Therefore, according to the invention of claim 6,
In addition to functioning equivalently to the above-mentioned invention, the sizing operation can be performed simultaneously in the granulation process of the sludge-like substance. The generation of granules becomes possible.

According to a seventh aspect of the present invention, in the first, second, third, fourth, or fifth aspect, at least one of the plurality of kneading blades is provided on a lower side surface of the main shaft. An extrusion-type kneading blade having a function of extruding an object to be granulated from the spindle side toward the tornado fin side is adopted.

Therefore, according to the invention of claim 7,
In addition to functioning equivalently to the invention described in the above-mentioned claims 1, 2, 3, 4 or 5, in addition to this, it is possible to always extrude a granulation target that tends to stay at the rotation center toward the tornado fin side. The kneading function can be further enhanced.

In the invention according to claim 8, in the granulating apparatus according to claim 1, at least one of the plurality of kneading blades is divided vertically. It is composed of two kneading plates equipped with different directions and an arm bar that fixes and holds this integrally, and
The upper kneading plate has a function of extruding the granulation object toward the tornado fin side, and the lower kneading plate has a function of extruding the granulation object toward the main spindle side. ing.

Therefore, in the invention according to claim 8,
In addition to functioning equivalently to the above-described claims 1, 2, 3, 4 or 5, the granulation object is further pushed out from the inner bottom of the casing toward the tornado fin side and dropped from above the tornado fin. The granulated object to be granulated can be pushed toward the main shaft side by the upper kneading plate, and at the same time, the granulated granulated object pushed into the main shaft side is again pushed out to the tornado fin side by centrifugal force or the like. In other words, in the course of such an operation, the kneading and granulation of the granulation target proceed at a stretch.

[0028]

DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to FIGS.

[First Embodiment] (Overall Configuration) First, in FIGS.
Indicates a cylindrical casing. In this casing 1,
A feeder (substance carry-in section) 2 for carrying in (injecting) the sludge-like substance that has been dehydrated into a cake is provided at the upper end.

Here, in FIG. 1, the feeder 2 is also used as a lime charging port.
As shown in (1), a lime inlet (lime feeder) 2A may be provided separately from the feeder 2. Further, each of the feeder 2 and the lime feeder 2A may be provided with an electromagnetically driven partition valve 2S as shown in FIG. 2 so that the opening and closing operation can be performed quickly as required.

In the casing 1, a spiral tornado fin 3 having substantially the same structure as that of the above-described conventional example is provided.
Are rotatably arranged along the inner wall of the casing 1. A main shaft 4 that holds the above-mentioned tornado fins 3 and that is driven to rotate integrally with the tornado fins 3 is rotatably mounted on a central shaft portion of the casing 1.

The reference numeral 3A designates the tornado fin 3 held at its lower end and the tornado fin 3 attached to the main shaft 4
2 shows a fin arm for fixing the fin arm. The fin arms 3A, the lower surface is disposed parallel to the inner bottom surface of the casing 1, the gap g ₁ is set to a size of approximately 1 [mm], for example.

When a predetermined amount of quicklime is added to a predetermined amount of the dehydrated cake and kneaded in the casing, the reaction between the water in the dewatered cake and the quicklime progresses, and granulation of the sludge-like substance is started. Simultaneously, when the tornado fins 3 are rotated at the same time, the dewatered cake that is being granulated rolls upward along the spiral surface of the tornado fins 3 to be granulated.

At the upper end on the inner wall side of the casing 1, FIG.
As shown in FIG. 9, a baffle plate 9 is provided corresponding to the upper end surface of the spiral surface of the tornado fin 3 described above. The baffle plate 9 has a function of sweeping down granular sludge-like substances rising along the spiral surface of the tornado fin 3. Here, FIG. 1 illustrates a case where one baffle plate 9 is provided, but FIG. 9 illustrates an example where two baffle plates 9 are provided at 180 ° intervals.

Further, on the upper end side of the casing 1, as shown in FIGS. 1 and 9, there is provided a granulated substance discharge section 11 provided with a discharge cover 11A for discharging the granulated sludge-like substance. (See FIG. 9). Further, an exhaust gas discharge section 12 that discharges exhaust gas in the casing 1 is provided at an upper end portion of the casing 1 (see FIG. 1).

In FIG. 1, reference numeral 13 denotes a spindle driving means for driving the spindle 4 in the casing 1. The main shaft driving means 13 is fixedly provided outside the bottom surface of the casing 1 described above, and is controlled by a controller 50 described later to rotationally drive the main shaft 4 at a predetermined speed. Code 13A
Denotes a spindle holding unit that holds the spindle 4 rotatably.

In the tornado fin 3 described above, the corners of the inner diameter side and the outer diameter side on the back side of the spiral surface are continuously cut off. This effectively prevents the sludge-like substance from adhering to the back corner of the tornado fin 3.

(About kneading blades) As shown in FIGS. 3 to 6, first to third kneading blades 5, 6, and 7 arranged along the bottom surface of the casing 1 are attached to the main shaft 4.
It is fixed and held on the rotation center side.

Among them, the first kneading blade 5 is shown in FIGS.
As shown in FIG. 4, the fin arm 3A protrudes from the main shaft 4 in the radial direction integrally with the fin arm 3A while being fixed on the fin arm 3A. The first kneading blade 5 has a function of pushing out the sludge-like substance remaining on the main shaft 4 toward the second kneading blade 6. Therefore, the first kneading blade 5 has a small turning radius and a relatively high height, whereby the first kneading blade 5 rotates integrally with the rotation of the main shaft 4, and the sludge positioned on the main shaft 4 side It has a function as an extrusion-type kneading blade that pushes the solid substance toward the outer tornado fin 3 side.

The second kneading blade 6 is shown in FIGS.
As shown in the figure, the mixing blades 5 are arranged on the downstream side at an interval of about 150 ° in the rotation direction of the kneading blade 5. here,
FIG. 5 shows the shape of the second kneading blade 6 as viewed from the direction of arrow B in FIG. This second kneading blade 6
The bottom surface is formed in an isosceles triangle shape having a point on the rotation direction side, and the rear end surface forms an isosceles triangle shape standing upright,
The upright upper end of the rear end face and the above-mentioned bottom end are connected linearly to form a ridge line.
a, 6b are formed.

The second kneading blade 6 is held on the bottom side by an L-shaped holding plate 6A. The L-shaped holding plate 6A is formed such that the front end region in the rotation direction is uniformly large and has an inclined surface.
Thereby, the second kneading blade 6 functions to scoop up the sludge-like substance located on the bottom surface side of the casing 1 and then to distribute the sludge-like substance to the left and right (to the center of rotation and the outer periphery of rotation).

Therefore, during operation, the main shaft 4 rotates at a predetermined speed, and at the same time, the first and second kneading blades 5, 6, the fin arm 3A and the holding plate 6
A, and the tornado fins 3 and the like shift to an integral rotation operation. In this case, when the lime for promoting solidification is simultaneously supplied, the kneading of the sludge-like substance is smoothly performed together with the start of the rotation of the main shaft 4.

The addition of lime or the like causes the generation of heat and the solidification of the sludge-like substance to proceed. In the process, as described later, the sludge-like substance starts to be granulated at a predetermined timing.
Here, when kneading, solidifying and granulating the sludge-like substance, in the case of the present embodiment, the third kneading blade 7 is also used.
Demonstrate predetermined functions.

As shown in FIGS. 3 and 6, one end of the third kneading blade 7 is fixed to the main shaft 4 described above.
The other end is formed of a plate member extending in the rotation radius direction, and the rotation end side is set wider than the above-described center side. Here, FIG. 6 shows the third kneading blade 7 as viewed from the direction of arrow C in FIG.

The third kneading blade 7 is set so that its tip end in the direction of rotation is slightly raised, and its rotating end is bent downward. Reference numeral 7A indicates the bent portion. Further, the third kneading blade 7 is provided with a plurality of relatively large through holes 7a on the entire surface thereof, and the sludge-like substance can escape through the plurality of through-holes 7a. Is made smoothly.

Further, in the third kneading blade 7, the lower edge of the bent portion 7A and the rear edge in the rotation direction are set to the same height g ₃ (with respect to the bottom surface of the casing 1).
In addition, irregularities (jaggies like saw blades) are formed on the lower end edge and the rear end edge in the rotation direction of the bent portion 7A. This allows the sludge-like substance to function as a perforated blade that can be appropriately fragmented (granulated) in the process of solidification of the sludge-like substance.

In this case, the height g ₃ of the lower edge and the rear edge in the rotational direction of the bent portion 7A is set to, for example, 6 [mm] in accordance with the intended particle diameter, but may be 5 [mm] or It may be 20 [mm] or may be set to an intermediate size.

(Regarding the large-grain chopping means) On the upper end side of the tornado fin 3, a large-grain chop for engraving the ascending granulated material into a predetermined size while rolling along the spiral surface of the tornado fin 3 is provided. Means 15 are provided.

As shown in FIG. 1, FIG. 7 and FIG. 8, the large grain engraving means 15 is disposed along the spiral surface of the tornado fin 3 described above, and is spaced apart from the tornado fin 3 by a predetermined distance. A plurality (four in FIG. 7) of fixedly mounted cutter members (needles with sharp tips) C ₁ , C
₂ , C ₃ and C ₄ . The cutter members C ₁ , C ₂ , C ₃ , and C ₄ rotate integrally with the tornado fin 3 described above.

The needle-shaped cutter members C ₁ , C ₂ ,
C ₃ and C ₄ may be provided at any place of the tornado fin 3 which is considered necessary, but in practice, the uppermost one is more convenient. For example, a rolling regulation unit (FIG. 1)
9 to 20, it is preferable that the flapper mechanism 35) is mounted in the upper direction of the rolling restricting means. The distance between the respective cutter members C ₁ -C ₄ and the side wall of the casing 1 mentioned above is gradually reduced set as it goes upward. This is shown in FIGS.

[0051] That is, the first sludge-like substance which is granulated with a large grain, first, somewhat cut by the cutter member C ₁ (FIG. 7
reference). Subsequently, as the member rolls upward, the cutter member C
_2, the C ₃ scraped little by little and finally the cutter member C
Set to final size by ₄ .

(About the small-diameter particle drop elimination mechanism) As shown in FIG. 1 and FIG.
A small-diameter grain drop elimination mechanism 18 that operates at a predetermined timing is provided. The small-diameter grain drop elimination mechanism 18 is, for example, provided with a rolling restriction means (flapper mechanism 35 in FIGS. 19 to 20) described later, and is mounted in the upper direction of the rolling restriction means.

As shown in FIG. 9, the small-diameter particle drop elimination mechanism 18 is provided with a cutout 18A formed by cutting off a part of the side wall of the casing 1 described above, and is disposed so as to fit into the cutout 18A. A side wall member 18B having the same shape and the same size as the cutout hole 18A, a side wall member drive mechanism 18C for moving the side wall member 18B outward in the radial direction of the casing 1 or returning the side wall member 18B to the original position;
The side wall member 1B is allowed to move and the side wall member 1
8B and a cover case 18D having a structure that covers the entire periphery of the above-described cutout hole 18A.

When the small-diameter grain drop elimination mechanism 18 is operated, the side wall member 18B is urged by the side wall member drive mechanism 18C to move outward along the radial direction of the casing 1 (see FIG. 1). Thus, the gap S between the outer periphery of the tornado fin 3 and the inner wall surface of the casing 1 is widened.

For this reason, a small-diameter granular material falls from the widened gap S. In this case, a configuration is adopted in which the target small-diameter particles are, for example, those having a diameter of 1/4 or less of the finally intended granular material. That is, in this case, the gap S is set to S = D / 4, where D is the diameter of the finally intended granular material.

When the small-diameter granule drop elimination mechanism 18 is actuated to drop and remove the small-diameter granules, the granulated material discharge unit 11 provided on the upper side surface of the casing 1 is actuated. I do.

(Regarding Granulated Material Discharge Portion) As shown in FIGS. 1 and 9, the above-described granulated material discharge portion 11 has the upper end side in FIG. 1 as a pivot point and is urged to drive means (not shown). A discharge cover 11A which is opened and closed and operates, and a granulated material guide portion 11B for guiding the granules to fall in a predetermined direction when the discharged cover 11A is set to the open state and the granulated material is discharged. It is provided with a configuration. In FIG. 1, the granulated material guide portion 11B is provided with the discharge cover 1 described above.
It has a structure that covers the entire 1A.

Here, reference numeral 11Ba denotes the granulated material guide portion 1.
Reference numeral 1C indicates a granulated material discharge port, and reference numeral 11C indicates a lid member that opens and closes the granulated material discharge port 11Ba (see FIG. 1).

The granulated substance discharged from the granulated substance discharge section 11 is conveyed by a conveyor belt 21 provided below, for example, as shown in FIG. 2, and passes through a necessary drying section and a measuring section. They are sequentially stored in a predetermined storage bag and packed.

(External Member of Casing, etc.) The above-described casing 1 is held by a holding frame 22. The holding frame 22 has legs 22A provided at four corners mounted on the floor via load cells LC. In this case, the load cell LC is
And a function of constantly outputting a signal corresponding to the entire weight of the casing 1 and the like of the holding frame 22 to a controller to be described later.

Further, as shown in FIG. 2, a pressure feed pump (for example, a displacement type) 24 for feeding predetermined air into the casing 1 and an air deodorizing means are provided at the upper end of the casing 1. Air sending means 26 for sending out to the outside through the air feeding means 25.

Here, the pressure pump 24 is used mainly for discharging steam generated by charging lime or the like from the inside of the casing 1. In this case, the pressure feed pump 24 may feed hot air into the casing 1. Further, the casing 1 described above may be configured to heat the casing 1 by steam or electric heat as necessary.

Alternatively, in the deodorizing means 25 and the air sending means 26 described above, without operating the pressure feeding pump 24, the deodorizing means 25 and the air sending means 26 are supplied to the outside by the vapor pressure generated when the water in the sludge-like substance is vaporized by the reaction heat. It may be configured to emit.

In FIG. 2, reference numeral 27 denotes a support frame. The support frame 27 is configured to hold the whole of the above-described dewatering cake feeder 2, the lime charging port (lime feeder) 2A, the air sending means 26 including the deodorizing means 25, and the pressure pump 24.

Here, the aforementioned dehydrated cake feeder 2,
As shown in FIG. 2, rubber bellows members 10 are interposed between the casing 1 and each of the lime charging port (lime feeder) 2A, the air sending means 26 including the deodorizing means 25, the pressure pump 24, and the like. Have been. This bellows member 10
Is internally sealed from the surroundings.

Thus, it is possible to effectively avoid applying unnecessary weight to the load cell LC that constantly outputs weight information, and to detect a change in weight inside the casing 1 immediately and accurately by the load cell LC. Has become.

In FIG. 1, reference numeral 29a denotes a spray nozzle for spraying a liquid binder such as water. The spray nozzle 29a is provided with a binder supplying means 29 (see FIG. 10) for supplying a liquid binder such as predetermined water via a pipe 29A. Then, the controller 50 operates as necessary to open and close the spray nozzle 29a, whereby the moisture content in the granulation target such as sludge-like substance can be adjusted.

(Regarding Drive / Control System) In FIG. 10, reference numeral 50 denotes a controller. The controller 50 controls the drive of the spindle 4 at a predetermined speed via the spindle drive means 13 described above. Also, this controller 50
A small-diameter particle exclusion timing setting for setting the small-diameter particle drop elimination mechanism 18 to an operating state after a lapse of a predetermined time after a predetermined amount of lime is added to the dehydrated cake in the casing 1 and the hydration reaction is started. Has functions. Further, after setting the operation state of the small-diameter particle drop elimination mechanism 18, the controller 50 controls the opening of the discharge cover 11 </ b> A of the above-described granulated substance discharge section 11 (see FIG. 9) via a driving unit (not shown). It has a cover opening control function.

Further, the above-mentioned casing 1 has an in-bath temperature sensor 30 for constantly measuring the temperature inside the casing 1.
A, an in-tank humidity sensor 30B that constantly measures the humidity in the casing 1, and a heater 28 that maintains the casing 1 at a predetermined temperature for a predetermined time are provided. The output information of the in-tank temperature sensor 30A, the in-tank humidity sensor 30B, and the in-tank pressure gauge 30C is constantly sent into the controller 30. Then, based on these pieces of information, the set temperature of the heater 28 is calculated according to a predetermined standard. In this case, if only kneading and granulation are intended, the small-diameter particle drop elimination mechanism 18 described above does not need to be particularly provided.

(Overall Functions, etc.) Next, overall functions, effects, and the like of the above embodiment will be described. Here, the above-mentioned sludge-like substance will be limited to a dewatered cake obtained by dewatering sewage sludge for convenience of explanation.

First, quicklime was added to a dewatered cake obtained by dewatering sewage sludge, and a hydration reaction “Ca0 + H ₂ O = Ca
(OH) ₂ +15.2 [kcal] ”and dehydration by water evaporation and compound formation due to heat generation. In this dehydration process, granulation and sizing are usually performed. In the present embodiment, the tornado fins 3 are used, and a large-grain notch means larger than a predetermined size and a drop-removal means for small particles that are too small are used. The feature is that it has. It is also characterized in that grains falling within a predetermined size range are taken out at a predetermined appropriate time for granulation.

Further, in the above embodiment, the water content after dehydration is about to be about 75 to 85%. The amount of lime input to the dehydrated cake varies depending on the moisture content of the dehydrated cake, the amount of CaO in commercial quicklime, and the like.

As described above, the main shaft 4 for rotating the tornado fins 3 is provided in the processing tank (casing 1) which enables processing such as kneading and sizing, and a lower portion of the processing tank (casing 1). The rotational force is given by the spindle drive means 13 depicted in FIG. The sludge-like material and the lime, which are the granulated materials, are charged from an input port (dewatering cake feeder 2A) in advance or in a batch while rotating. Here, the controller 50 first receives information from the load cell LC,
The amount of the granulation target in the casing 1 is calculated (FIG. 11,
Step S1).

In the tornado fins 3, the granulated material (granulated object) is initially moved upward by the tornado fins 3, and the baffle plate 9 or the rolling restricting means (for example, the flapper in FIGS. The mechanism 35) returns to the main shaft 4 side (central portion) and falls, and this state is returned to perform kneading (FIG. 11, step S2). Here, when the granulation target is a powder, the binder supply means 29 is immediately activated to activate the spray nozzle 29a.
, And a kneading operation is started after appropriately adding water and a binder.

When the water content of the granulated material becomes appropriate, the kneading operation shifts to the granulating operation, and the spiral surface of the tornado fin 3 becomes a rolling surface to promote granulation (FIG. 11). , Step S3). In this case, the rolling control means (for example, the flapper mechanism 35 in FIGS. 19 to 20) functions to bridge the rolling of the granulation target upward.

In this granulation stage, the controller 50
Activates the small-diameter grain drop elimination mechanism 18. Thereby, a substance (granulated substance) smaller than a predetermined diameter is dropped, and the particles are combined to have an appropriate particle diameter. Cutters C _{1 to} C ₄ are provided in the middle of the tornado fin 3,
Larger particles have a given diameter (eg, about 6 mm)
And gradually ascending (FIG. 11, step S
4).

The particles pass through the small-diameter particle drop elimination mechanism 18, are sized, and are discharged to the outside without falling. Here, the timing of the opening / closing operation of the discharge cover 11A is controlled by the controller 50, and the granulated material discharge unit 11 is opened after the start of the granulation process (FIG. 11, step S5). After the 2 discharge, after the drying process and the like, the product becomes a final product after bagging. FIG. 11 shows a series of these operation steps.

When the granulated material is discharged, the controller 50 calculates the weight of the granulated object in the casing 1 based on the information from the load cell LC again as described above, and prepares the next granulated material to be prepared. To grasp the quantity of goods (Fig. 11,
Step S6).

This method is characterized in that the fin arm 3A and the tornado fin 3 and the self-cleaning action in the processing tank (casing 1) can withstand long-term batch processing. It is also an important element of the kneading blade 7 to have a function of breaking large lumps that cannot lift the tornado fins 3 (during the rotation, tearing or crushing at the uneven portion on the lower edge).

The controller 50 determines the granulation timing based on the weight information from the load cell LC for measuring the weight of the entire apparatus. That is, the amount of water evaporation can be monitored, and the determination can be made at a predetermined weight loss. In addition, the reaction heat can be monitored, and it can be judged from the transition of the temperature rise (since the required amount of water evaporation is proportional to the amount of heat generation). There is also a good possibility that only the elapsed time from the lime input is sufficient.

Further, the suitable time for granulation is, for example, when the dehydrated cake having a water content of about 80% is reacted with quicklime to release the steam generated in the stirring tank (casing 1) to the outside. It can be obtained in advance by an experiment from the obtained information shown in FIG. These data are stored in a memory (not shown), and are used by the controller 50 as timing setting for starting the operation of the small-diameter particle drop elimination mechanism 18 or timing setting for starting the discharging operation of the granulated material discharging unit 11.

In order to ensure that the granulation is carried out, in the above-described method, the water content of the granulated material (granulation target), the structure for promoting the granulating action on the material, the appropriate kneading speed, and the tornado fin length The selection of parameters such as height is important.
Regarding the moisture content of the granulated material, the treatment tank (casing 1)
There is a big change depending on the structure. That is, since it depends on whether or not the structure actively condenses steam, based on the structure, an appropriate amount of lime is added to the dehydrated cake, and after a lapse of a predetermined time after the start of the hydration reaction, it is suitable for granulation. It is necessary to consider the water content.

When the moisture content of the dehydrated cake varies greatly, it is important to take a small amount of lime and take measures to reduce the moisture other than the hydration reaction. For the material with a low water content, lime is added, and for the material with a high water content, measures to reduce the water content are directly heated or performed by hot air blowing, and at the same time, the water content is reduced using the load cell LC described above. The rate can be measured and appropriate measures can be taken based on this.

In the above-described embodiment, the internal air (steam) is adjusted to a predetermined water content by the pressure pump.
Or the hot air or steam is pumped from the outside, and when the granulating member reaches an appropriate moisture content, the pumping or suction is stopped.

Here, how to determine that the water content has reached the appropriate value will be described. As described above, FIG. 2 shows an example of connection between the processing tank (casing 1) and the external unit. The rubber bellows 10 is provided for the purpose of isolating gravity so that the unit thereabove does not load the load cell LC. The dewatered cake feeding amount DW [kg] is measured by the load cell LC, and a lime amount SW [kg] corresponding thereto is added, and the grain discharge port 11Ba is closed.

In one example, the steam generated by the reaction heat causes a pressure increase and is discharged through the deodorizing section 12, and a part of the generated steam is condensed in the processing tank (casing 1) to form the material to be granulated. Increase the moisture content. When the generated steam is in such a state, the calculation of the water content in the processing tank is performed by the controller 50 based on the change in the weight data obtained from the load cell LC.
Executed in Then, when the water content reaches the appropriate water content, it is used as the timing setting of the operation start of the small-diameter particle drop elimination mechanism 18 or the timing setting of the discharge operation start of the granulated material discharge unit 11 as described above.

In the above-described embodiment, the load torque applied to the spindle drive motor changes significantly between the case where the granulated substance (granulated material) is cake-shaped and the case where the granulated substance is granulated.
For example, 20 minutes after the start of the reaction with lime, if the granulated material is in the form of a cake, a slight predetermined amount of lime is added, and then 20 minutes.
For about a minute or so, turn on the heater for the first time (O
N).

Further, in the above embodiment, the case where the sludge material is targeted as the material to be granulated is exemplified. However, for example, a material obtained by adding an appropriate aqueous binder to powder to form a cake, etc. If it is a dehydrated cake-like substance, it can be applied to other substances other than the sludge substance as it is.

As described above, in the above embodiment, the granulation effect by kneading is doubled by the kneading blade and the tornado fin 3, and the rolling surface of the tornado fin 3 rolls while the grain rolls and rises. It is configured to crush large grains, so that even if the amount of treatment in the tank is large, the sludge-like substance (granulation target) that has been dewatered and caked can be efficiently kneaded and granulated and sized. Can be.

Further, since the tornado fins are provided with the large-grain chopping means 15 for sizing, granulation and sizing can be performed without changing the size of the entire apparatus. As compared with the conventional example that requires a large number of devices, the entire device can be reduced in size and multifunctional.

For this reason, in the case of agricultural chemicals, fertilizers, ceramics, etc., powder (fine dust) or dehydrated cake is formed into granules or granules,
This prevents scattering (reduces the loss of scattering and does not pollute the work environment) and increases the bulk density (storage, supply, packaging,
Easy handling in transportation, etc.), prevention of aggregation, deterioration and adhesion,
There is an advantage that it is possible to improve the appearance, improve the fluidity (no bridging phenomenon of the granulated object in the hopper) and the like.

[Second Embodiment] Next, a second embodiment will be described with reference to FIGS. In the second embodiment, the above-described kneading blade (see FIGS. 3 to 6)
3 shows another example.

First, in FIG. 13, reference numeral 31A denotes an extrusion-type kneading blade. The symbol K indicates the rotation direction of the main shaft 4. Here, the extrusion-type kneading blade 31A described above is used.
Is connected and held on the fin arm 3 </ b> A and below the main shaft 4, and extends along the tangential direction of the main shaft 4 and downstream in the rotation direction of the main shaft 4. Thereby, the granulation target that tends to stay on the lower side surface of the main shaft 4 is moved to the main shaft 4.
It functions so as to push out from the side toward the tornado fin 3 side. And in this case, the extrusion-type kneading blade 31A
Is set somewhat higher than the carry-in height of the granulated object (eg, cake-like sludge-like substance) carried in.

Further, the lower part of the main shaft 4 is set at α degrees (approximately 130 degrees) from the tip of the extrusion type kneading blade 31A.
°) An inclined surface type kneading blade 32B is provided on the downstream side in the rotation direction at a distance (see FIG. 14). The inclined surface type kneading blade 32B includes a holding plate 32Bc protruding from the lower portion of the main shaft toward the tornado fin 3, and a kneading member 32 standing upright on the entire surface of the holding plate 32Bc in the rotation direction.
Ba, 32Bb.

Here, of the kneading members 32Ba, 32Bb, one of the kneading members 32Ba is provided with an inclined surface on the main shaft 4 side. The other one stands in a state where the outside of the tip in the rotation direction is bent in the direction of about 60 ° (= θ) toward the downstream side in the rotation direction K with respect to the tip of the holding plate 32Bc described above. The standing surface 32Bb is provided. Except for the extrusion-type kneading blade 31A and the inclined-surface-type kneading blade 32B, other configurations are the same as those in the case of FIG. 3 described above.

For this reason, the kneading blades 31A and 32B of the second embodiment rotate the main shaft 4 in the K direction, and at the same time, the extrusion-type kneading blade 31A moves the granulated object on the main shaft 4 side from the main shaft 4 side. Push it out toward the tornado fin 3 side.

Subsequently, when the granulation target is kneaded, a part of the granulation target is formed on the inclined surface 3 of the inclined surface type kneading blade 32B.
After being pushed upward along 2Ba, the mixture is again stirred to slide down to the main shaft 4 side. At the same time, a part of the granulation target is extruded toward the tornado fin 3 by the upright surface 32Bb. Other configurations and operations are the same as those of the above-described first embodiment.

Therefore, the second embodiment (FIGS. 13 to 15) has the same operation and effects as those of the first embodiment, and in particular, the inclined surface 32Ba of the inclined surface kneading blade 32B. In this point, the granulation target can be kneaded while moving the granulation target up and down, and in such a point, the kneading can be performed more quickly and effectively while moving the granulation target along the rotational radius direction. There is.

Third Embodiment Next, a third embodiment will be described with reference to FIGS. The third embodiment shows still another example of the kneading blade (see FIGS. 3 to 6) in the first embodiment described above.

First, in FIG. 16, reference numeral 33A denotes an extrusion-type kneading blade 31A according to the second embodiment.
3 shows the same extrusion-type kneading blade. The symbol K indicates the rotation direction of the main shaft 4.

In the third embodiment, α degrees (approximately 130 degrees) from the tip of the extrusion-type kneading blade 33A described above.
°) A two-way kneading blade 34 equipped with two kneading blades is provided downstream and separated therefrom. The two-way kneading blade 34 is composed of two kneading plates 34A and 34B having the same width, which are separately provided vertically, and an L-shaped holding arm 34C for integrally fixing and holding the kneading plates 34A and 34B. here,
The height of the upper kneading plate 34A is set substantially the same as that of the lower kneading plate 34B, but may be different. Also, one of the widths may be set longer than the other.

The upper kneading plate 34A constituting the two-way kneading blade 34 is fixedly mounted on the above-mentioned L-shaped holding arm 34C with its surface slightly facing the main shaft 4. Thereby, when the main shaft 4 rotates in the K direction, the upper kneading plate 34A forcibly removes the granulation target from the main shaft 4 described above.
It works to push it out to the side. That is, during operation, the upper kneading plate 34A has a function of pushing out the granulation target toward the main shaft 4 side.

The lower kneading plate 34B constituting the two-way kneading blade 34 is fixedly mounted on the above-described L-shaped holding arm 34C with its surface facing the slightly outside tornado fin 3 side. Thus, when the main shaft 4 rotates in the K direction, the lower kneading plate 34B functions to forcibly push the granulation target toward the tornado fin 3 described above. That is, during operation, the lower kneading plate 34B has a function of pushing out the granulation target toward the tornado fin 3 side.

For this reason, in the present embodiment, the extrusion-type kneading blade 33A and the two-way kneading blade 34 function simultaneously, so that the granulation target is effectively kneaded and granulation is started, and the tornado is formed. Upward rolling on helical surface on fin 3 and variable baffle plate mechanism 37
The process of kneading and granulation effectively proceeds by the downward drop caused by the movable baffle plate 37A (see FIG. 21). The arrow R shown in FIG. 18 indicates the movement path of the granulation target in this case. Other configurations and operations are described in the first embodiment (FIGS. 1 to 1).
It is the same as 2).

Therefore, the third embodiment (FIGS. 16 to 18) has the same operation and effect as those of the first embodiment described above, and in particular, the operation of the main shaft 4 by the operation of the two-way kneading blade 34. The granulation target can be circulated and moved by utilizing the entire space between the side and the tornado fin 3, and at this point, the kneading and granulation of the granulation target are performed more quickly and effectively. There is an advantage that can be.

[Fourth Embodiment] Next, a fourth embodiment will be described with reference to FIGS. The fourth embodiment is provided at a predetermined position on the helical surface of the tornado fin 3 in the first embodiment described above, and the granulated material rolling from below along the continuous helical surface is interposed. It shows a flapper mechanism 35 as a rolling restricting means devised to fall, and is characterized in that it is provided on a part of the spiral surface of the tornado fin 3.

The flapper mechanism (rolling restricting means) 35 shown in FIGS.
Bridging plate (flap fin) 3 which constitutes part of
5a, a driving support shaft 35A that holds the bridging plate 35a and urges the bridging plate 35a to move up and down in a direction along the surface of the tornado fin 3, and performs a predetermined operation on the driving support shaft 35A. Energized spindle drive unit 3
6.

[0108] Reference numeral 3K denotes a cut-out portion formed on the spiral surface of the tornado fin 3 for dropping particulate matter. Then, the above-described bridging plate 35 covering the cut portion 3K is described.
a is arranged.

More specifically, the driving support shaft 35A
Holds one end of the above-described bridging plate 35a at one end thereof (on the lower surface side), and the other end thereof penetrates the side surface of the above-mentioned tubular main shaft 40 so as to be rotatable about the main shaft 40. Is held.

Further, the above-described spindle drive unit 36 is provided with a main shaft 40.
It comprises a wide pinion gear 36A mounted on the inner drive support shaft 35A, and a round rack 36B meshed with the pinion gear 36A. Among them, round rack 36
B is provided so as to be able to move up and down within the main shaft 40, and it is possible to arbitrarily change and move the moving distance by external operation.

FIG. 20 shows the operation of the bridging plate (flap fin) 35a, and shows a state in which the support shaft driving unit 36 is operated to raise the bridging plate 35a. In this case, the length of the helical surface of the tornado fin 3 is shortened, and the granulated object falls down from the helical surface after being rolled and ascended, so that the action of the kneading blade is effectively performed. Will receive it. For this reason, kneading and granulation of the granulation target are performed in a relatively short time, and the spiral surface of the tornado fin 3 can be set substantially short, so that the load on the power source driving the tornado fin 3 is reduced. Therefore, a large amount of material (granulation target) can be processed.

Further, the flapper mechanism 3 in this embodiment
Reference numeral 5 indicates that since the tornado fins 3 are partially cut out and formed so that they can be turned up and down, the tornado fins 3 can be substantially shortened or lengthened, and a method of use depending on the granulation process can be selected. Can be set. Further, versatility can be further improved in that the operation stop of the flapper mechanism 35 can be easily selected and set from outside.

That is, in the flapper mechanism 35, the bridging plate 35a is controlled by the above-described controller 50 as necessary to swing up and down. When the rotating end is raised, the bridge plate 3
5a prevents the granulated material from being scooped up (rolled) upward along the spiral surface of the tornado fin 3, and drops from the cutout 3A into the casing 1.

For this reason, at the stirring time during the kneading / granulation process, the bridging plate 35a is raised to connect the paths from the granulation time (ie, the flapper mechanism 3).
5 is not operated) and the kneading and granulating speed is set to an optimum low speed, while the flapper mechanism 35 is operated to shorten the length of the spiral surface of the tornado fin 3 (reducing the rotational load). The rotation speed of the tornado fins 3 is increased, thereby making it possible to increase the kneading, granulating, and sizing speeds and reduce the size of the entire apparatus. The other configuration and operation and effect are the same as those of the first embodiment.

[Fifth Embodiment] Next, a fifth embodiment will be described with reference to FIGS. The fifth embodiment prevents the granulated sludge-like substance from rolling upward in the predetermined position on the spiral surface of the tornado fin 3 in the first embodiment described above. Alternatively, it is characterized in that a variable baffle plate mechanism 37 as an allowable rolling restriction means is provided. Reference numeral 41 denotes a tubular main shaft that rotationally drives the tornado fin 3.

The variable baffle plate mechanism (rolling restricting means) 37 shown in FIGS. 21 and 22 is a movable baffle which is retractably disposed at a predetermined position on the main shaft 41 side from the spiral surface of the tornado fin 3 described above. A plate 37A, one end of which is fixed to the main shaft 41 and the other end of which is a tornado fin 3
And a fixed arm 37B rotatably holding the movable baffle plate 37A at the other end, and reciprocating in a direction substantially parallel to the fixed arm 37B and along the length thereof. A drive arm 37C for urging the tornado fin 3 to rotate by the drive arm 37C;
The cam mechanism 38 drives the 7C.
The cam mechanism 38 is provided inside the main shaft 41.

More specifically, the movable baffle plate 37A is disposed close to the spiral surface of the tornado fin 3 and in a state of rising on the spiral surface.
The rear end (on the side of the main shaft 41) is arranged in the direction of the main shaft 41 while being slightly separated from the tornado fins 3. The fixed arm 37B has a rotation support shaft 37Ba parallel to the above-described main shaft 41 at the distal end thereof. And this rotating spindle 3
The movable baffle plate 37 with 7Ba as a rotation center axis.
A is held rotatably.

The drive arm 37C has one end thereof connected to the main shaft 4A.
1 and the one end is engaged with the cam mechanism 38 of the main shaft 41 described above. The other end of the drive arm 37C extends slightly from the front end of the movable baffle plate 37A to the rear end of the movable baffle plate 37A.
The movable baffle plate 37A is rotatably connected to an upper end surface portion of the movable baffle plate 37A via a pin 37Ca provided in parallel with 7Ba.

Therefore, when the drive arm 37C moves toward the main shaft 41 along its axis, the movable baffle plate 37A moves from its solid line to the position shown by the two-dot chain line, as shown in FIG. 21, for example. As a result, the movable baffle plate 37A is retracted from the spiral surface of the tornado fin 3.

The above-described cam mechanism 38 includes a drive arm 37.
C is urged to move along its axis. As shown in FIG. 22, the cam mechanism 38 has a thick plate-like cam plate 38A, holds the cam plate 38A down inside the main shaft 41, and urges the cam plate 38A to move up and down. And a drive support shaft 38B.

Further, as shown in FIG. 22, the cam plate 38A has an inverted V-shaped guide through-hole 38Aa whose lower part is cut obliquely downward in a direction away from the drive arm 37C from the center. Is formed. The guide arm 37C is inserted into the guide through-hole 38Aa.
A guide pin 37Ca fixed to one end of the guide pin 37Ca is provided. Thereby, when the cam plate 38A moves up and down, it is guided by the guide through hole 38Aa and
7Ca moves, and the reciprocating movement of the drive arm 37C in the direction along its axis is urged. Reference numeral 37Cf denotes a working through hole for incorporating the guide pin 37Ca.

For this reason, in the fifth embodiment, the movable baffle plate 37A can be freely disposed at a predetermined position on the spiral surface of the tornado fin 3 by an external operation. Is advantageous in that the movable baffle plate 37A can always be arranged at the optimum position.

Further, in the fifth embodiment, the length of the spiral surface of the tornado fin 3 can be substantially shortened as in the case of FIGS. For this reason, kneading can be performed at an optimally low speed, and the granulating and sizing speed can be increased. The other configuration and operation and effect are the same as those of the first embodiment.

In each of the above embodiments, a band heater may be provided around the outer wall of the reaction tank (casing 1) to adjust the water content. Further, for adjusting the water content, steam may be sent into the tank, water may be sprayed, or hot air or external air may be sent.

[0125]

Since the present invention is constructed and functions as described above, according to the present invention, a granulation object such as sludge-like substance which has been dewatered and caked is formed by rolling with a kneading blade and a tornado fin. And, for example, for sludge-like substances having a high water content, the rolling control means is operated to substantially shorten the length of the spiral surface of the tornado fins and to roll upward. To reduce the number of rotations of the tornado fins to promote kneading, and at the same time, stop the operation of the rolling control means from the middle to make the length of the spiral surface of the tornado fins longer,
Thereby, various operations can be performed according to the water content of the dewatered cake, such as accelerating the functions of kneading and granulation, so that the versatility can be further enhanced, and in this respect, the size of the entire apparatus can be increased. Kneading, granulation, and sizing can be performed without changing the size, and the size reduction and multi-functionalization of the entire device can be achieved as compared with the conventional example that requires a large number of installation places by installing a sizing device. For this reason, powders (fine dust) or dehydrated cakes are formed into granules or granules in pesticides, fertilizers, ceramics, etc., thereby preventing scattering (reducing the loss of scattering and not polluting the working environment).
And increase of bulk density (easiness of handling in storage, supply, packaging, transportation, etc.), prevention of aggregation, deterioration and adhesion, improvement of appearance, and improvement of fluidity (no fridge phenomenon in hopper). Thus, it is possible to provide an excellent granulating apparatus that has never been achieved before.

[Brief description of the drawings]

FIG. 1 is a partially omitted schematic longitudinal sectional view showing a first embodiment of the present invention.

FIG. 2 is an explanatory diagram showing an example of an exterior of a casing in the first embodiment of FIG. 1;

FIG. 3 is an explanatory view showing each kneading blade provided on the inner bottom portion of the casing in the first embodiment of FIG.

FIG. 4 is an explanatory diagram showing a shape of a first kneading blade and a positional relationship with a main shaft in FIG. 3;

FIG. 5 is an explanatory diagram showing a shape of a second kneading blade in FIG. 3 and a positional relationship with a main shaft.

FIG. 6 is an explanatory diagram showing a shape of a third kneading blade in FIG. 3 and a positional relationship with a main shaft.

FIG. 7 is an explanatory view showing an example of a large-grain notch means provided in a casing in the embodiment of FIG. 1;

FIG. 8 is an explanatory diagram showing an operation of the cutter along a line BB of the large grain engraving means disclosed in FIG. 7;

FIG. 9 is an explanatory diagram showing the structure of a small-diameter particle drop elimination mechanism provided in the casing of the first embodiment in FIG. 1 and a positional relationship with the casing.

FIG. 10 is a block diagram showing an example of various sensors provided in the first embodiment in FIG. 1 and an example of a control system including them and a controller.

FIG. 11 is an explanatory diagram (flowchart) showing the operation procedure of FIG. 1;

FIG. 12 is a diagram (measured value) showing a temperature change of the dewatered cake when a predetermined amount of lime is put into the dewatered cake (dewatered sludge).

FIG. 13 is a partially sectional front view showing an example of a kneading blade portion in the second embodiment.

FIG. 14 is a partially omitted plan view of FIG. 13;

FIG. 15 is a schematic explanatory view showing a kneading blade portion viewed from the right direction in FIG. 14;

FIG. 16 is a partially sectional front view showing another example of a kneading blade portion in the third embodiment.

FIG. 17 is a partially omitted plan view of FIG. 16;

FIG. 18 is an explanatory view showing the operation of the kneading blade portion disclosed in FIG.

FIG. 19 is a partially sectional plan view showing a flapper mechanism according to a fourth embodiment.

20 is an explanatory diagram showing the operation of the flapper mechanism in FIG.

FIG. 21 is an explanatory diagram showing a variable baffle plate mechanism in the fifth embodiment.

FIG. 22 is a partially cutaway front view showing the variable baffle plate mechanism disclosed in FIG. 21;

FIG. 23 is an explanatory view showing a conventional example.

[Explanation of symbols]

DESCRIPTION OF SYMBOLS 1 Casing 2 Material carrying-in part 3 Tornado fin 3A Fin arm 4, 40, 41 Main shaft 5 First kneading blade as an extrusion type kneading blade 6 Second kneading blade 7 Third kneading blade as a perforated blade 9, 44 Baffle plate 11 Granulated substance discharge section 11A Discharge cover 12 Exhaust gas discharge section 13 Main shaft drive means 31A, 33A Extrusion type kneading blade 32B, 34 Kneading blade 34A Upper kneading plate 34B Lower kneading plate 34C Arm bar 35 Flapper as rolling control means Mechanism 35a Bridge plate 35A Drive support shaft 36 Support shaft drive unit 37 Variable baffle plate drive mechanism as rolling restriction means 37A Movable baffle plate 37B Fixed arm 37C Drive arm 38 Cam mechanism 50 Controller

──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Shigeo Takayama 2-16-46 Minami Kamata, Ota-ku, Tokyo Inside Tokimec Co., Ltd. (72) Yoshio Abe 2-16-46 Minami Kamata, Ota-ku, Tokyo Inside Tokimec Co., Ltd. (72) Inventor Yasuo Abe 2-16-46 Minami Kamata, Ota-ku, Tokyo Inside Tokimec Co., Ltd. (72) Mutual Takahashi 2--16-46 Minami Kamata, Ota-ku, Tokyo Stock Company (56) References JP-A-7-136696 (JP, A) JP-A-61-230731 (JP, A) JP-A-4-131500 (JP, U) (58) Fields surveyed (Int. Cl. ⁷ , DB name) B01J 2/10 C02F 11/00

Claims (8)

(57) [Claims] 1. A cylindrical casing provided with a substance carry-in section for carrying a predetermined amount of sludge-like substance dewatered into a cake, and a spiral tornado rotatably disposed along an inner wall of the casing. A fin, a main shaft arranged at a central shaft portion of the casing, for holding the tornado fin and rotating the tornado fin, a plurality of kneading blades fixed and held to the main shaft, and an upper end in the casing A fixed baffle plate that sweeps up particulate matter that rises along the spiral surface of the tornado fins, and a granulated substance discharge unit that is provided at a predetermined location on the side surface of the casing and discharges granulated sludge-like substance. ,
An exhaust gas discharge unit that discharges exhaust gas in the casing, wherein the casing is provided with a spindle driving unit that rotationally drives the spindle, at a predetermined position on a spiral surface of the tornado fin, The dirt
Activated when the water content of the mud substance is high the sludge-like substance before
A granulating device comprising a rolling restricting means for preventing the spiral surface from rolling upward. 2. The granulating apparatus according to claim 1, wherein said rolling restricting means is constituted by a flapper mechanism formed by forming a part of said tornado fin so as to be able to move up and down. 3. The flapper mechanism according to claim 1, further comprising: a bridging plate forming a part of the tornado fin; holding the bridging plate; and giving the bridging plate an up-and-down rotation in a direction along a surface of the tornado fin. 3. The granulating apparatus according to claim 2, wherein said granulating device comprises a driving spindle for urging and a spindle driving unit for urging the driving spindle for a predetermined operation. 4. The variable baffle plate mechanism according to claim 1, wherein said rolling restricting means is a variable baffle plate mechanism having a baffle plate removably disposed at a predetermined position on a spiral surface of said tornado fin. Granulation equipment. 5. A movable baffle plate disposed at a predetermined position on a surface of the tornado fin, a movable baffle plate provided at a predetermined position on the surface of the tornado fin, and one end of the movable baffle plate rotatably held inside the tornado fin. A fixed arm having a portion fixed to the main shaft, a drive arm disposed substantially parallel to the fixed arm and biasing the tornado fin to rotate by reciprocating movement along a central axis; and a driving force applied to the drive arm. 5. The granulating apparatus according to claim 4, wherein said granulating apparatus comprises a cam mechanism for urging the main shaft, and said cam mechanism is provided in said main shaft. 6. The granulating apparatus according to claim 1, wherein at least one of the plurality of kneading blades is a perforated blade having a sizing function. . 7. An extrusion-type kneader, wherein at least one of the plurality of kneading blades is provided on a lower side surface of the main shaft and has a function of pushing out a granulation target from the main shaft side toward the tornado fin side. The granulator according to claim 1, 2, 3, 4, or 5, wherein the granulator is a blade. 8. At least one of the plurality of kneading blades is composed of two kneading plates vertically and diagonally divided and an arm bar for integrally fixing and holding the kneading plates. The upper kneading plate has a function of extruding the granulation object toward the tornado fin side, and the lower kneading plate located on the lower side has a function of extruding the granulation object toward the spindle side. The granulation apparatus according to claim 1, 2, 3, 4, or 5, wherein