KR20000077346A - Drying apparatus - Google Patents

Abstract

The present invention relates to a container (1) capable of charging a dried object and a stirring provided in the container in a dryer for making a dried product solid by agitating and heating a dried material exhibiting coagulation property in a drying process. A hard mass 11 having blades 3A, 3B and 3C and stirred together with the object by stirring blades 3A, 3B and 3C is housed in the container 1. In the forward rotation of the stirring blades 3A, 3B, and 3C, the dry matter is scraped into the drying treatment area (a), and in reverse rotation, the conveying function of sending the dry matter to the drying area (c) opposite to the drying treatment area (a) is provided. Have

Description

Dryer {DRYING APPARATUS}

BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a dryer in which water is evaporated from a wet waste, a wet waste fermentation in a liquid or mud shape, or a dried matter such as sludge generated in sewage treatment, and the dried matter is a solid dry matter. The present invention relates to a drier in which a dried material exhibiting coagulation property in a drying process becomes a solid dried material by stirring and heating in a container.

Conventionally, in this type of dryer, the agitation for the dry matter in the vessel was dependent only on the stirring blades.

However, in the conventional machine as described above, the dry matter generally has a property of solidifying sequentially in the course of drying thereof, and due to the solidification property, the dry matter adheres to each part or stirring blade in the container, Phenomena such as solidification in the accumulated state and solidification into large masses in the container appeared. As a result, there is a problem in that the solid dry matter after the drying treatment is taken out or the operation of the dryer itself is disturbed.

In addition, maintenance work to remove solids adhered to the container is often necessary for the same reason, which is expensive in maintenance management and practically cannot be used in small facilities where full-time managers are difficult to deploy.

In view of the above circumstances, the main problem of the present invention is to effectively solve the above problems by simple improvement. In other words,

[1] A dryer according to claim 1 of the present invention,

A hard mass having a container into which the dry object is to be charged and a stirring blade provided in the container, which are stirred together with the dry object by the stirring blade, is housed in the container.

That is, according to the above structure, the hard mass is stored in the dried material which is solidified in order by solidification along the progress of drying by stirring the hard mass contained in the container with the dry matter in the container with the stirring blade. Subsequent collisions cause the solidified dry matter to be effectively crushed. By the pulverizing action, the dry matter is effectively prevented from adhering to the respective parts or stirring blades in the container and solidifying in the accumulated state or solidifying into a large mass in the container.

As a result, the phenomenon such as taking out the solid dry matter after the drying treatment from the container or disturbing the operation of the dryer can be effectively avoided. As a result, the dryer which can perform a drying process smoothly and stably is provided, Furthermore, in the maintenance work in order to remove the solid substance adhered in a container, the said minimum required frequency is significantly reduced at least, and the said maintenance work This content becomes simpler, and in some cases, maintenance work becomes unnecessary.

Nevertheless, the dried material to be solidified is pulverized more effectively than the hard mass, so that the solid dry matter after the natural drying treatment becomes a homogeneous particulate form or powder form, so that the solid dry matter after the drying treatment can be smoothly carried out, Handling of the solid dry matter after removal is also quite easy.

In addition, the improvement cost is also low because the material is simply improved by simply storing a hard block of a suitable size in a container.

[2] In the present invention according to claim 2 of the present invention, in the practice of the invention according to claim 1,

The container is a cylindrical container arranged in the transverse direction, the cylindrical container is provided with a drying treatment area and a take out area, the stirring blade is a rotary blade that rotates relative to the cylindrical container around the center of the cylindrical container, The stirring blade scrapes the dry matter in the cylindrical vessel into the drying treatment region in the forward rotation, and reversely rotates the dry matter in the cylindrical vessel into the ejecting region in the center direction opposite to the drying treatment region. A regulating means is provided, which has a conveying function and which restricts the mass from entering the ejecting area.

That is, according to the said structure, by carrying out a drying operation by rotating the said rotating blade positively, the said dried blade carries out stirring and scraping together the to-be-dried object to the dry process area | region in a container with a hard mass, and a drying process area | region It is possible to reliably and effectively collide the hard mass with the dry matter to be accumulated in the dry matter, and to perform a pulverizing function, thereby further facilitating atomization or granulation and homogenization of the solid dry matter after the drying treatment.

Then, after the drying operation, by rotating the rotary blade reversely, the solid dried material after the drying treatment can be sent to the area to be taken out from the drying treatment area by the rotary blade, and can be taken out of the container at the dry product outlet of the area to be taken out. That is, taking out the solid dry matter after a drying process can be performed only by the simple operation which changes the rotation direction of a rotating blade. Moreover, by this, the structure which can implement the automation of an extraction process easily is obtained.

In addition, taking out the solid dry matter is carried out by using a rotary blade to stir the dry matter, so that the structure is simpler compared to the configuration of a separate conveying means exclusively taken out, a compact apparatus is obtained, and the apparatus cost is also low. Will be done.

Furthermore, when the rotating blade is rotated in reverse, it is sent in the direction of the hard mass and the takeout area together with the solid dry matter after the drying treatment, but the entry of the hard mass into the takeout area is regulated by the restricting means, so the reverse rotation of the rotating blade Regardless, the hard mass is retained in the container, and after the solid dry matter is taken out, when the rotary blade is rotated forward, the hard mass is returned to the drying treatment area by the rotating blade.

[3] In the invention according to claim 3 of the present invention, in the practice of the invention according to claim 2,

The said regulating means is the inside of a cylindrical container WHEREIN: It is characterized by the partition arrange | positioned between a drying process area | region and a taking out area | region.

That is, according to this structure, the situation where the water contained in the to-be-injected object which was put into the drying process area | region flows in the horizontal direction inside the cylindrical container in the transverse direction to the center direction, and leaks out of a container from a drying outlet is the said partition. By being prevented by water, the water contained in the to-be-dried is reliably evaporated by the heat-drying process, maintaining in the drying process area | region by the said partition, and the said generated vapor flows out to a predetermined | prescribed discharge location. As a result, a dryer which is more excellent in terms of hygiene or environmental preservation is provided.

[4] In the invention according to claim 4 of the present invention, in the practice of the invention according to claim 3, an isolation region is provided between the drying treatment region and the extraction region, and the partition is the drying treatment. A main partition provided between the area and the isolation area, and a partition height provided between the isolation area and the takeout area, from the secondary partition having a lower height than the main partition; The rotating blade which rotates between the said main partition and the said auxiliary partition is provided in order to transfer water to the said drying process area | region, The opening part which takes out the solid dry matter after a drying process is formed in the bottom part of the said extraction area | region.

That is, according to the above configuration, the dried material leaked into the isolation region, or water contained therein, or the hard mass in the separation region when the container is put into the container or in the stirring process or the like is separated by the rotating blade of the isolation region. The drying process can be effectively advanced by stirring together with a hard mass while heating a to-be-dried material, for example, by heating means, such as an electric heater, making it move to a dry process area | region. When the drying operation is completed, the respective rotating blades are rotated in reverse to send the solid dried material after the drying treatment to the area where the primary partition and the auxiliary partition are sequentially taken out from the drying processing area by the respective rotary blades, and the dried material can be taken out from the discharge port. have.

1 is a block diagram of a wet garbage disposal apparatus according to the present invention.

Fig. 2 is a side view showing the supporting structure of the collision mechanism of the wet waste disposal apparatus.

3 is a plan view showing a support structure of the collision mechanism of FIG.

4 is a block diagram of a water level detection device of the wet waste disposal apparatus.

5 is a control circuit diagram of a water replenishment valve of the wet waste disposal apparatus.

6 is a timer flowchart showing an opening and closing control mode of the water refill valve of FIG. 5.

Figure 7 is a longitudinal sectional view of the dryer for the present invention.

8 is a cross-sectional view of the dryer of FIG. 7.

(Configuration of Wet Garbage Disposal Device)

The wet waste disposal apparatus shown in FIG. 1 includes a decomposition tank 41 for decomposing wet waste by aerobic bacteria in stored water, a wet waste input device 42, and decomposition residues. It is made to dry as a to-be-dried thing, and has a dryer 66 called an odorless small piece material S in a solid dry matter. Opening the lid 42a of the wet waste discharging device 42, putting the wet waste into the apparatus, and then operating the dispensing switch (not shown), the conveyed water Wc passes through the conveyed water supply path 43. While being supplied to the input device 42, the pulverization / conveying pump provided in the wet waste input device 42 is operated. Accordingly, the crushed wet waste is sent to the decomposition tank 41 through the input passage 45 together with the conveyed water Wc.

The decomposition tank (liquid tank) 41 has air (Ai) in the air region 48 in the reservoir located on the reservoir surface of the decomposition tank 41 by an induction effect due to the discharge wind Af of the exhaust fan 47 49, the water discharger (ejector) 46 discharged to the outside and the fine water droplets contained in the discharged air Ai from the air region 48 in the reservoir tank to collect the collected water 41 A water separation device 50 for returning back to the inside and an air inlet 51 are provided to introduce external fresh air Ao into the air region 48 in the reservoir according to the air discharge.

In addition, the main circulation path (W) for storing the water stored in the reservoir (W; the water stored in the reservoir containing the material or decomposition debris during the decomposition) through the intake port 53 of the lower decomposition tank 41 by the circulation pump 54 ( 52) is installed. Part of the water (Wa) flowing out by the main circulation path 52 is classified into the watering branching path 55 and discharged from the discharge port 56 above the decomposition tank 41 to the air region 48 in the water storage tank. The other part (Wb) of the water (W) is separated into the agitation branch (57), and returns to the decomposition tank (41) through a return port (58) disposed on the opposite side to the intake port (53).

In addition, at the time of wet waste injecting, another part of the outflowed water W becomes the above-mentioned conveyed water Wc by opening of the automatic valve 59 based on the operation of the inlet switch, thereby supplying the conveyed water. Through the furnace 43, the classification and feeding to the wet waste input device 42.

A collision mechanism 60 is installed directly under the drain port 56, and the discharge water Wa discharged downward from the drain hole 56 collides with the collision mechanism 60 in the air region 48 of the reservoir. It scatters. The collision mechanism 60 has a truncated conical shape. As a result, the discharged water Wa from the drain port 56 is returned to the water W stored in the reservoir in a state where the discharge water Wa is scattered in the air region 48 in the reservoir, whereby the scattered water Wa is the air inlet 51. The air is efficiently contacted with the air Ai in the air region 48 in the reservoir containing fresh air Ao sucked in from, and as a result, oxygen is efficiently supplied to the water W stored in the reservoir.

Further, when the water W stored in the intake port 53 is removed, the stirring of the stored water W in the reservoir based on the return from the intake port 58 and the water W stored in the reservoir by the stirrer 61 are performed. Stirring is performed while efficiently supplying oxygen by the scattered water, whereby oxygen evenly spreads over the entirety of the stored water W in the reservoir. As a result, in the stored water W, decomposition of wet garbage is promoted by aerobic bacteria, and at the same time, generation of odor due to promotion of the aerobic decomposition is prevented.

The structure which supports the collision mechanism 60 in the air region 48 in a reservoir may be implemented in the form shown in FIG. 2 and FIG. That is, the fixed tube part 62 is fixed to the ceiling member of the disassembly tank 41, and the opening of the front end of the fixed tube part 62 forms the drain port 56. As shown in FIG. Each of the four members 63 extends from a part of the base of the fixed tube portion 62. Each of the four members 63 is disposed at equal intervals around the lower region of the drain port 56. Between the lower ends of each of the four members 63, a support plate 64 which is always immersed in the stored water W is provided. And, from the upper surface of the support plate 64, a straight strut 65 concentric with the drain port 56 is provided, and a collision mechanism 60 is attached to the upper end of the strut 65.

Thus, the collision mechanism 60 is provided in the upper end part of the support | pillar 65 provided from below, and the substance in the process of decomposition | disassembly mixed with the discharge water Wa from the drain opening 56, and decomposition | disassembly waste (especially fibrous Is caught in a location between the drain port 56 and the collision mechanism 60, and is prevented from being deposited. As a result, a situation in which the state of scattering due to the collision with the collision mechanism 60 of the discharge water Wa discharged from the drain port 56 due to the above-described deposits becomes poor, or the situation in which the drain port 56 is blocked. Is prevented.

In addition, the lower end of each member 63, which is a support device for supporting the strut 56, is disposed in the stored water W, so that the strut 65 is an air region in the reservoir above the stored water W. By being protruded toward the 48, the substance (the substance during dispersing or the decomposing residue) caught on the support 65 or each member 63 is stored in the water stored along the surface of the support 65 or each member 63 ( W) sinks and disperses in stored water (W). As a result, the deposit phenomenon at the point between the drain port 56 and the collision mechanism 60 is prevented, and maintenance for the removal of a deposit is unnecessary, or it can effectively reduce.

In order to return the outflowed water Wb of the other part from the return port 58 into the reservoir, a discharge path 67 is formed in the stirring branch 57 to send the decomposition residue to the dryer 66. A portion Wb 'of the outflowed water Wb, which flows out from the intake port 53 and is sent to the stirring branch 57 in a state where decomposition is sufficiently advanced, is sent to the dryer 66 through the discharge path 67. . In the dryer 66, the decomposed residues in the outflowed water Wb 'are heated and dried to a temperature at which carbonization occurs, to form a crunchy semi-carbonized, odorless small piece substance S and recovered in the recovery container 68. The amount of odorless small piece material (S) generated in this way corresponds to about 1 to 3% of the amount of wet waste put.

The agitation branch 57 is provided with an automatic valve 72 for taking out the decomposed waste. The discharge path 67 is also provided with an automatic valve 73 for taking out the debris.

In the normal circulation state, the automatic valve 72 on the side of the agitation branch 57 is opened, the automatic valve 73 on the side of the discharge path 67 is closed, and the spilled water sent to the agitation branch 57 is closed. The total amount of (Wb) returns from the return port 58 into the reservoir. From the said normal circulation state, when the automatic valve 72 of the side of the stirring branch 57 is closed first, the branch point of the discharge path 67 will remain in the residual amount Wb of the water discharged | emitted from the stirring branch 57. What is further upward automatically flows downward and returns from the return port 58 into the reservoir. Subsequently, when the automatic valve 73 on the discharge path 67 side is opened, the outflowed water Wb 'remaining above the automatic valve 73 in the discharge path 67 is supplied to the dryer 66.

In other words, in the state where the decomposition of the wet waste in the decomposition tank 41 has sufficiently proceeded, the operation of the automatic valves 72 and 73 is repeated at regular time intervals so that the longitudinal discharge path 67 is used as a meter. In the form, a certain amount of outflowed water Wb 'including decomposed waste is supplied to the dryer 66 at regular intervals, and the heat drying treatment of the decomposed waste in the dryer 66 is continuously performed.

Moreover, the water level detection for detecting the water level of the water replenishment valve (liquid supply valve) 74 which opens and closes the replenishment channel 75 to replenish the water in the digester 41 and the stored water W in the digester 41. The device 76 and the like are installed. By controlling the opening and closing of the water replenishing valve 74 based on the water level detection information of the water level detecting device 76, the water level of the stored water W in the decomposition tank 41 is adjusted to be maintained at the set water level ML.

As shown in FIG. 4, the water level detection device 76 applies air Ap pressed through the air supply 78 to the detection tube 77 and the detection tube 77 arranged in the longitudinal direction. It has an air pump 79 (supply means) to supply and the pressure switch 81 (pressure detection means) operated ON / OFF according to the internal pressure P of the detection tube 77 by the water level information. The detection port 77a formed at the lower end of the detection tube 77 is immersed in the stored water (W). The internal pressure P of the detection tube 77 is guided to the pressure switch 81 through the pressure passage 80. In the state of supplying air to the detection tube 77 by the air pump 79, the pressure P in the tube decreases in accordance with the change in the water level (pressure of the stop head), and finally the pressure P in the tube reaches the set water level ( The pressure switch 81 is configured to be ON when it becomes smaller than the set value Ps corresponding to ML), that is, when the water level of the stored water W becomes lower than the set water level ML.

In addition, a valve controller (valve control means) 82 is provided in the operation control device 87 of the decomposition tank 41 to control the opening and closing of the water replenishment valve 74 based on the ON / OFF of the pressure switch 81. In the effective control, the valve controller 82 moves the water replenishment valve 74 to the next stop control after opening only the predetermined valve opening time Ta when the pressure switch 81 is turned ON. In the following, the water replenishment valve 74 is kept closed only for a predetermined stop time Ta regardless of the ON / OFF of the pressure switch 81, and then the next effective control is moved. In this form of control, the effective control and the stop control are configured to repeat each other.

Specifically, the valve controller 82 is composed of two circuits provided between the power supply lines 84a and 84b, as shown in FIG. The first circuit includes a parallel connection circuit of the relay contact r1 and the pressure switch 81, and the parallel connection circuit is provided between the contact 83a of the twin timer 83 and the relay coil R. Is connected in series. The second circuit is a circuit in which the relay contact r2 and the solenoid 74a of the water replenishment valve 74 are connected in series.

Thereby, as shown in FIG. 6, first, by the operation of the twin timer 83, the timer contact 83a is maintained in the ON state and the stop time (for the period of the effective time T1 (for example, 3 minutes). T2; for example 3 hours), the OFF state maintained for a period of time is repeated. The period during which the timer contact 83a is kept ON is an effective control period. Then, when the pressure switch 81 is turned on (that is, when the internal pressure P is less than the set value Ps) during the ON period (time T1) of the timer contact 83a, the timer contact 83a is released from that time. The time Ta until it becomes OFF becomes the said predetermined valve opening time Ta. During the predetermined valve opening time Ta, the water supplement valve 74 is placed in the valve opening state regardless of the next ON / OFF of the pressure switch 81. On the other hand, the period in which the timer contact 83a is turned off is a stop control period. During the period (time T2) during which the timer contact 83a is kept OFF, the water replenishment valve 74 is kept in the valve open state regardless of the ON / OFF state of the pressure switch 81.

As a result, the following effects are obtained by the valve control form as described above. That is, hunting on the ON / OFF operation of the pressure switch 81 based on the periodic fluctuations in the pressure P of the pipe caused by the water wave generated by the stirring of the stored water W or the discharge operation of the air pump 79. Even when hunting occurs, hunting does not reach until opening and closing of the water supplement valve 74. In addition, in the decomposition tank 41, the water replenishment valve 7 is opened only at a predetermined valve opening time Ta for the reduction of the stored water W by the discharge from the evaporator or the dryer 66. The water level of the stored water (W) at is automatically adjusted to the set water level (ML).

As shown in FIG. 4, in the detection tube 77, a water jet tube 85 (liquid jetting means) is built in, and the jet port 85a provided at the lower end of the water jet tube 85 has a detection tube 77. Is opened toward the detection port 77a from the tube. The branch water passage 86 is connected to the water jet pipe 85 by a decomposition tank 41 in the refill channel 75 further branched from a portion downstream from the water refill valve 74. Thus, in the control of the water level, a portion Wf 'of the replenishment water Wf fed from the water replenishment valve 74 at the time of valve opening of the water replenishment valve 74 is the tip of the water jet pipe 85. It blows off with the water for cleaning from the jet port 85a. The water jet prevents accumulation of substances during decomposition in the stored water W, decomposition debris or scale deposition, etc. in the detection port 77a.

Further, the operation control device 87 performs operation control of the grinding / conveying pump, the circulation pump 54, the stirrer 61, and the dryer 66, and at the same time, the automatic valve 59 in the conveying water supply path 43. Control of the opening and closing of the automatic valves 72 and 73 for supplying fixed amount of waste to the dryer 66. In addition, the operation control device 87 is a temperature of the stored water (W) based on the stored water temperature detected by the temperature sensor 88 for the heat generation due to decomposition of wet waste, the set temperature (for example 40 ° C.) The output of the exhaust fan 47 is controlled to be maintained at.

Further, the water level detecting device 76 is provided with a pressure gauge 89 that displays the intra-pipe pressure P of the detection pipe 77 guided by the pressure induction path 90.

Moreover, the intake path 91 which connects the inside of the wet refuse input device 42 and the air area | region 8 inside the decomposition tank 41 is connected. As the air inside the wet waste injecting device 42 is sucked through the intake path 91 in accordance with the discharge of the air Ai in the decomposition tank by the exhaust fan 7, the odor is emitted from the wet waste injecting device 42. This is avoided.

In addition, an exhaust path 92 is provided between the dryer 66 and the air region 48 inside the decomposition tank 41. As the exhaust air (Ai) in the digestion tank is discharged by the exhaust fan (7), the generated gas (mainly water vapor) from the dryer (66) passes through the exhaust path (92) in the air region (8) in the digestion tank (41). The water vapor in the generated gas is condensed and recovered in the cracking tank 41 as much as possible by being introduced into it, and only the non-condensing gas portion is discharged from the exhaust port 49 to the outside together with the air Ai in the cracking tank.

(Configuration of Dryer)

7 and 8 show an example of the configuration of the dryer according to the present invention. The dryer 66 has a cylindrical container 1 having a center P which is horizontal (an example of the transverse direction) and a plurality of rotating blades 3A, 3B, 3C (an example of stirring blades) provided in the cylindrical container 1. Have The rotary blades 3A, 3B, 3C are all driven rotationally by a motor 6 extending radially outward from the center P and one rotation shaft 2 disposed on the center and connected to the rotation shaft 2. do. In this embodiment, the cylindrical container 1 is fixed not to rotate. The inlet port 5 is formed in the ceiling of the cylindrical container 1, and the outflowed water Wb 'containing decomposition | disassembly waste as a to-be-dried object is thrown in from the inside into the cylindrical container 1 from here.

In addition, in the lower half of the cylindrical container 1, a plurality of electric heaters 4 are arranged to heat the dry matter (that is, decomposition waste) in the cylindrical container 1. Thereby, the to-be-dried material thrown in into the container 1 from the inlet 5 is heated with the electric heater 4, stirring by rotation of the rotary blades 3A, 3B, 3C, and the odorless small piece substance S as a solid dry matter. It becomes The electric heater 4 is rod-shaped extended in parallel with the center P, and a part of the cross section is provided in the state which is buried in the outer peripheral surface of the cylindrical container 1.

The inside of the cylindrical container 1 is divided into the drying process area | region a, the isolation | separation area | region b, the extraction | ejection area | region c, etc. in the center P direction. A main partition 7 is provided at the boundary between the dryer processing region a and the isolation region b, and an auxiliary partition 8 is provided at the boundary between the isolation region b and the extraction region c. Both the primary partition 7 and the secondary partition 8 are provided to protrude upward from the bottom of the cylindrical container 1, and the secondary partition 8 has a height higher than that of the primary partition 7. Is set low. In addition, at the bottom of the take-out area c, a dry matter discharge port 9 is formed to take out the solid dry matter after the drying process. In addition, the inlet 5 is provided in the drying process area a.

That is, when the dry matter is injected from the inlet 5 into the drying process area a, the main partition 7 and the auxiliary partition 8 contain the container from the dry outlet 9 with the water contained in the dry matter as a stain. To prevent it from leaking out. And the water contained in the to-be-dried evaporates by the drying process by heating and agitation, maintaining water in the drying process area | region a by the main partition 7, and the vapor | steam generate | occur | produced in this way of the cylindrical container 1 It is discharged out of the cylindrical container 1 from the gas outlet 10 which is arrange | positioned adjacent to the inlet 5 in the ceiling. The steam is further discharged from the gas outlet 10 to a predetermined discharge point.

In the cylindrical container 1, a plurality of hard blocks 11 of appropriate sizes are accommodated. This hard mass 11 is agitated simultaneously with the object to be dried by the rotary blades 3A, 3B, and 3C. At the time of the stirring, the hard mass 11 is pulverized efficiently to dry the solidified object by causing the dry matter to collide with the dry matter to be solidified. By the pulverizing action, the dry matter adheres to and accumulates in the solid form on each portion or the stirring blades 3A, 3B, and 3C starting from the inner wall of the cylindrical container 1, or the dry matter is formed into a large mass in the container. Solidification is effectively prevented. The hard mass 11 may be formed of, for example, a metal sphere or a ceramic sphere. In addition, the outer diameter of the hard mass 11 is the smallest gap formed between the rotating trajectories of the rotating stirring blades 3A, 3B, and 3C and the inner wall of the cylindrical container 1, or the rotating trajectories and partitions. It is set to a dimension sufficiently larger than the smallest gap formed between (7, 8).

The structure of each rotating blade 3A, 3B, 3C is explained in full detail. The rotary blades 3A, 3B, and 3C are composed of the main rotary blade 3A installed in the drying treatment place a, the intermediate rotary blade 3B provided in the isolation region b, and the exit rotation installed in the takeout region c. It is comprised from the blade 3C.

First, the main rotary blade 3A is installed side by side along the center P such that the stirring zone extends to the entire length of the drying treatment area a with respect to the center P direction, that is, four sets of main rotary blades 3A, namely And a first main rotating blade 3A ', a second main rotating blade 3A2, a third main rotating blade 3A3, and a fourth main rotating blade 3A'. The first main rotary blade 3A 'is close to the one end cover 1a farthest from the isolation area b of the cylindrical container 1, and the fourth main rotary blade 3A' is located at the isolation area b. Placed in close proximity. Referring to the first main rotating blade 3A 'as an example, the first main rotating blade 3A' includes a pair of attachment rods 21 and 21 extending in the radially opposite direction from the rotation shaft 2, It consists of a plate 31 extending so as to be slightly inclined with the center P from the tips of the attachment rods 21 and 21. In other words, the two plates 31 and 31 of the first main rotating blade 3A 'are in the same position with respect to the center P direction, but constitute a pair arranged so that the mutual rotation phases are shifted by 180 degrees. . The rest of the main rotating blades 3A2, 3A3, 3A 'also has the same attachment rods 22, 23, 24 and plates 32, 33, 34 fixed thereto. However, in the attachment rods adjacent to each other in the direction along the center P, that is, the attachment rod 21 and the attachment rod 22, and the attachment rod 23 and the attachment rod 24 are mutually rotated in phase It is arrange | positioned so that it may shift by 90 degrees.

Tip of each plate 31, 32, 33, 34 of the first main rotating blade 3A ', the second main rotating blade 3A2, the third main rotating blade 3A₃, and the fourth main rotating blade 3A'. The site is close to the inner circumferential surface of the cylindrical container 1. Further, with respect to the rotary blades 3A located at both ends of the drying treatment area a, that is, the first main rotary blade 3A 'and the fourth main rotary blade 3A', the side edges are formed in a cylindrical container ( It is comprised so that it may rotate in the state adjacent to the inner surface of the one end side cover 1a of 1), or the wall surface of the main partition 7.

Next, the intermediate rotary blade 3B of the isolation region b is the center P from the tip of the pair of attachment rods 25 and the attachment rods 25 extending radially opposite from each other from the rotation axis 2. And a plate 35 extending to be inclined greatly. The two plates 35 of the intermediate rotary blade 3B also constitute a pair of blades disposed at the same position with respect to the center P direction but arranged so that mutual rotation phases are shifted by 180 degrees. The side edges of the pair of blades 35, 35 rotate in a position close to the wall of the primary partition 7 and the wall of the auxiliary partition 8.

Further, the exit rotary blades 3C in the take-out area c are centered from the ends of the pair of attachment rods 26 and attachment rods 26 extending radially opposite from each other from the rotary blades 2. And plate 36 extending to be slightly inclined. The two plates 36 of the outlet rotating blades 3C also constitute the pair of blades which are disposed at the same position with respect to the center P direction, but arranged so that mutual rotation phases are shifted by 180 degrees. The side edges of the pair of blades 36, 36 rotate the position close to the inner surface of the other end cover 1b of the cylindrical container 1 and the wall surface of the auxiliary partition 8.

Moreover, the plate 35 of the intermediate rotary blade 3B of the isolation region b is formed of the fourth main rotary blade 3A 'in the drying treatment region a which rotates in a state close to the main partition 7. It is provided in the state which rotated about 90 degrees with respect to the plate 34. And the plate 36 of the exit rotation blade 3C of the extraction | release area | region c is a state where rotation angle shifts only a predetermined angle with respect to the plate 35 of the intermediate rotation blade 3B of the isolation | separation area | region b. Is installed.

As shown in Fig. 8, each plate 31, 32, 33, 34, 35, 36 of each of the above-mentioned rotating blades 3A, 3B, 3C is subjected to the forward rotation indicated by the solid arrow in Fig. 8. In both of the edges with respect to the center P direction, the rear edge (edge on the side of the other end cover 1b) rotates ahead of the front edge in the rotational direction, and forward in the reverse direction to the container center direction. The side edge (side edge on the side of the one end cover 1a) is inclined so as to rotate earlier in the rotational direction more than the rear side edge. By the inclination, a forwarding function is generated in which forwarding of the dried object to the container front side (one end cover 1a side) occurs with the stirring function in the forward rotation, and in the reverse rotation, the dried object is returned to the rear side of the container (the other end cover 1b). Return function occurs.

That is, in the above-described structure, in the drying operation, each of the rotating blades 3A, 3B, and 3C is rotated forward so that the dry matter or hard mass 11 in the drying treatment region a is formed in the drying treatment region a. It is thoroughly scraped toward the front of the cylindrical container 1 by the main rotating blade 3A, and when it is put into the cylindrical container 1 or beyond the main partition 7 by the stirring process or the like, in the isolation area b. The leaked dry matter or water and hard mass 11 contained therein is moved to the drying treatment area a beyond the main partition 7 by the intermediate rotating blade 3B of the isolation area b. Simultaneously with this series of operations, the drying process proceeds by heating the dried object with the electric heater 4.

Then, when the above drying operation is completed, the respective rotary blades 3A, 3, B 3C are reversely rotated so that the solid dried material after the drying process is removed from the drying treatment region a by the respective rotary blades 3A, 3B, 3C. The main partition 7 and the auxiliary partition 8 are sequentially sent to the area c for taking out and flow out from the dry outlet 9.

In other words, each of the rotary blades 3A, 3B, and 3C causes the dry matter on the side of the ejecting area c in the cylindrical container 1 to pass over the partitions 7 and 8 in the forward rotation so as to dry matter processing area a. In the reverse rotation, the object to be dried on the drying treatment region a side in the cylindrical container 1 is sent to the region c which takes out the partitions 7 and 8 to have a function of exceeding the partition.

In addition, the dry matter discharge port 9 has a structure (for example, a lattice structure) through which the hard mass 11 cannot pass, and when the solid dry matter is taken out by reverse rotation of each rotating blade 3A, 3B, 3C. The hard mass 11 moved to the take-out area c is returned to the drying treatment area a by rotating the rotary blades 3A, 3B, and 3C after taking out the solid dried matter.

[Other Embodiments]

The following illustrates another embodiment of the present invention.

In the above embodiment, the main partition 7 and the auxiliary partition 8 are provided between the drying treatment region a and the drying outlet 9 to bring the edges closer to the walls of the partitions 7 and 8. The intermediate rotating blades 3B, which are rotated in the middle, between the two partitions 7 and 8 in the isolation region b, thereby allowing the dried material leaked from the isolation region b or the water contained therein to be separated from the isolation region b. Although it thickened and made the function which moves to the dry process area a high, the structure which abbreviate | omitted the auxiliary partition 8 is also possible.

In the case where the dry matter contains little water, the main partition 7 and the auxiliary partition 8 are omitted. In the forward rotation, the dry matter is thickened in the drying treatment area a while It is also possible to configure the equipment, which is only a rotary blade having a conveyance function for sending a dry matter (solid dry matter after the drying treatment) to the dry matter outlet 9.

The specific shape / structure required for the rotating blades in order to have the above-mentioned conveying function for the dried object or to allow the rotating blade to have a function of passing the partition to the dried object can be changed in various ways. It is not limited to the shape / structure illustrated in the above-mentioned embodiment.

In the above-mentioned embodiment, the structure which rotates agitation blade (rotating blade) 3A, 3B, 3C with respect to the fixed container (cylindrical container 1) is illustrated. However, on the contrary, it can also be set as the structure which rotates a container with respect to the fixed stirring blade, or the structure which rotates both by rotating a container and a stirring blade in a reverse direction.

Although the above embodiment exemplifies a form in which the rotary blades 3A, 3B, and 3C are embedded in the cylindrical container 1 in the transverse direction, in the practice of the invention according to claim 1, the specific shape / structure of the container is Various modifications are possible, and the stirring blade is not limited to the rotary type, for example, various types of stirring blades such as a swinging type stirring blade can be used.

In the above embodiment, an example of heating the dry object in the container by an electric heater is exemplified, but various kinds of heating apparatuses can be used, such as heating the heated object in the container by a burner.

The hard block 11 housed in the container is not limited to a metal sphere or a ceramic sphere, and may be a polyhedron other than spherical in shape. In addition, in the above materials, various kinds of materials may be used as long as they have a higher hardness than the solidified dry matter.

The dry object to be treated can be applied to various kinds of materials such as wet waste, wet or waste liquid fermentation in the form of liquid or mud, or mud form generated in sewage treatment.

Claims (4)

In the drier which makes a dried thing which agglomerates in the drying process the solid thing which agglomerates shows by stirring and heating, And a stirring blade (3A, 3B, 3C) provided in the container (1) and the container (1) capable of charging the dried material, the blood by the stirring blade (3A, 3B, 3C) The hard mass 11 which is stirred with the dry matter is housed in the container 1. dryer. The method of claim 1, The said container 1 is a cylindrical container arrange | positioned in the horizontal direction, In the said cylindrical container 1, the drying process area | region a and the extraction area | region c are provided, and the said stirring blades 3A, 3B, and 3C are And rotating blades 3A, 3B and 3C which rotate relative to the cylindrical container 1 around the center P of the cylindrical container 1, wherein the stirring blades 3A, 3B and 3C are at the forward rotation. The dry matter in the cylindrical container 1 is scraped into the drying treatment area a, and in the reverse rotation, the dry matter in the cylindrical container 1 and the dry processing area a in the direction of the center P. The regulating means which sends to the said taking out area | region c of the opposite side, has a conveyance function, and regulates that the block 11 enters the said taking out area | region c is provided. dryer. The method of claim 2, The regulating means has partitions 7, 8 arranged between the drying treatment area a and the take-out area c inside the cylindrical container 1. dryer. The method of claim 3, wherein An isolation region b is provided between the drying treatment region a and the extraction region c, and the partitions 7 and 8 are provided between the drying treatment region a and the isolation region b. The secondary partition 8 is provided between the primary partition 7 and the isolation region b and the extraction region c, and the partition height is lower than that of the primary partition 7, and the isolation region b A rotating blade 3b rotating between the main partition 7 and the auxiliary partition 8 to move the dry matter and the water contained therein to the drying treatment area a. In the bottom part of the said taking out area | region c, the dry matter discharge port 9 which takes out the solid dry matter after a drying process is formed. dryer.