JP6235253B2 - Waste treatment equipment - Google Patents

Description

  The present invention relates to a waste treatment apparatus (sealed fermentation drying apparatus) for treating organic waste such as livestock excrement and food residues and a waste treatment method using the apparatus.

  Organic waste such as livestock excreta discharged from livestock management bodies and food residues discharged from food industry establishments has increased in recent years, and their disposal has become a major social issue. ing. When these wastes are incinerated, the cost is high and there is a problem of dioxin generation. In addition, when landfilling is performed, there are problems of securing an exhaust location and odor damage. In addition, in recent years, the promotion of the reuse of organic waste has been demanded by legislation such as the Food Recycling Law. In view of these points, organic waste is composted and recycled as a recycling resource. Even when composting, organic wastes such as food residues have a high water content, so if they are not sufficiently dried and fermented, they may have a large volume and weight and may be spoiled.

  For this reason, in recent years, organic waste has been dried and composted using a closed fermentation drying apparatus (also referred to as “component”) that utilizes the fermentation action of microorganisms. This component has a cylindrical vertical tank shape, and is a composting device having a sealed vertical structure in which input waste does not easily come into contact with outside air.

  Conventionally, as a food residue fermentation treatment apparatus with excellent air permeability, food residues and aerobic microorganisms are mixed in an airtight vertical container, and the action of aerobic microorganisms while aeration and stirring inside the container Has proposed a device for fermenting food residues (see Patent Document 1). In this fermentation treatment apparatus, a plurality of upper and lower stirrer blades are radially extended around a rotating shaft standing in a vertical container, and a plurality of vent holes are drilled below the lowermost stirrer blade. The air is vented into the container through the vent. Examples of the shape of the stirring blade in this apparatus include a blade shape and a rod shape, and in particular, a screw type having a blade-shaped stirring blade is described from the viewpoint of stirring efficiency. Furthermore, this patent document 1 describes a fermentation treatment method in which the amount of aeration per unit time is larger than usual.

  In addition, an organic waste treatment apparatus for obtaining biogas that can be subjected to anaerobic fermentation treatment of the fermentation residue after anaerobic fermentation after anaerobic fermentation of the organic waste in the fermenter has been proposed ( Patent Document 2). In this organic waste treatment apparatus, similarly to Patent Document 1, a plurality of upper and lower stirrer blades are provided around a rotating shaft standing in the fermenter, and a plurality of vent holes are formed in the lowermost stirrer blade. The ventilation hole is ventilated into the fermenter. The shape of the stirring blade in this apparatus is a substantially mountain shape having a swash plate on the front side in the rotation direction.

JP 2010-69477 A JP 2011-121042 A

  As in Patent Document 1 and Patent Document 2, stirring means including a stirring blade is indispensable in a closed fermentation drying apparatus. However, depending on the shape of the agitating blade and the operation method, the load applied to the agitating blade, the rotating shaft, and the like becomes too large, and there is a possibility that these parts are partially damaged. Moreover, sufficient stirring performance cannot be obtained, and there is a possibility that poor fermentation may occur, and the time required for drying and composting may be prolonged. In the apparatuses of Patent Document 1 and Patent Document 2, the influence on the stirring performance is not studied regarding the shape of each stirring blade (each stage). Moreover, the stirring means of such a closed fermentation drying apparatus is an extremely low speed operation (about one rotation in 40 to 60 minutes), and the organic waste that is a processed product is solid, liquid, and semi Since it is a complex mixture containing a liquid substance etc., the prediction of stirring performance is not easy.

  In addition, malodorous substances such as ammonia generated by composting are caused by decomposition of organic substances, and the generation thereof is uncontrollable. For this reason, it is necessary to attach a deodorizing device and a deodorizing tank to the closed-type fermenting and drying device, which is a cause of increased production costs due to capital investment in livestock farmers and the like. Patent Document 1 describes that the drying rate is increased by increasing the air flow rate, but depending on other factors such as the air flow rate range and the shape of the stirring blade, a sufficient effect cannot be obtained. There is also a risk of poor fermentation due to a decrease in the temperature of the processed product.

  The present invention has been made in order to cope with such problems, has high stirring performance, hardly causes poor fermentation, can reduce the processing time of drying and composting of organic waste, An object of the present invention is to provide a waste treatment apparatus and a waste treatment method capable of reducing the generation amount.

  The waste treatment apparatus of the present invention comprises a vertical container, a rotary shaft provided in the vertical direction in the container, a plurality of stirring blades fixed around the rotary shaft, and external air in the container. A waste material taken out from the lower part of the container by fermenting, drying and composting the organic waste introduced from the upper part of the container into the container with agitation and stirring with the stirring blade In the material processing apparatus, the agitating blades are spaced apart from each other at a predetermined interval from the lower part to the upper part of the rotary shaft in the container, and at least one or more at each stage, from the rotary shaft. A linearly extending toward the inner wall of the container, and a lower agitation blade communicated with the air supply means, and a vent hole for introducing outside air sent from the air supply means into the container. The stirring blade has an inclined surface on the front side in the rotation direction. The inclination angle of the uppermost stirring blade with respect to the rotation surface of the stirring blade is less than 90 degrees, and the inclination angle of the lowermost stirring blade with respect to the rotation surface of the stirring blade. The inclination angle of the stirring blades other than the uppermost stage and the lowermost stage with respect to the rotating surface of the stirring blade is inclined with respect to the rotating surface of the stirring blade in the inclined surface of the lowermost stirring blade. The angle is greater than or equal to and less than or equal to the angle of inclination of the inclined surface of the uppermost stirring blade with respect to the rotation surface of the stirring blade.

  Here, the “stirring” of the organic waste in the present invention mixes organic waste (including solid, liquid, semi-liquid, etc.) composed of various constituents with fermentation and drying. This means a stirring and mixing operation.

  The uppermost stirring blade is characterized in that the central line of the width of the stirring blade does not pass through the axis of the rotating shaft when viewed from the vertical upper side of the rotating shaft.

  The inclination angle of the uppermost stirring blade with respect to the rotation surface of the stirring blade is 55 to 65 degrees, and the inclination angle of the lowermost stirring blade with respect to the rotation surface of the stirring blade is 15 degrees. It is ˜25 degrees.

The waste treatment method of the present invention is characterized in that organic waste is composted using the waste treatment apparatus of the present invention. Further, in the waste treatment apparatus, the air flow rate (m ³ ) per minute introduced into the container by the air feeding means is adjusted to ¼ to 1/2 of the internal volume (m ³ ) of the container. Then, aeration and agitation are performed. Further, the static pressure of the air supply means is 25 kPa or more. In addition, the outside air sent from the air feeding means is heated to 60 ° C. or more and introduced into the container.

  The waste treatment apparatus of the present invention includes an airtight vertical container, a rotary shaft provided in the vertical direction in the container, a plurality of stirring blades fixed around the rotary shaft, An aeration means for sending outside air to the container, and the agitating blades are spaced apart at a predetermined interval from the lower part to the upper part of the rotating shaft in the container, and at least one or more sheets are rotated at each stage. Rotating the agitating blade on the premise that the shaft is linearly extended from the shaft toward the inner wall of the vessel, and the lowermost agitating blade has a vent hole for introducing outside air from the air supply means into the vessel. With respect to the inclination angle of the inclined surface on the front side in the direction, the uppermost stage is set to be twice or more (less than 90 degrees) than the lowermost stage, and other than the uppermost stage and the lowermost stage are set to the lowermost stage and the uppermost stage. With this configuration, the treatment blade (waste) can be easily flattened and the contact area with the outside air can be increased by the stirring blade having a high inclination angle at the uppermost stage, and the contact area with the outside air can be increased. With the stirring blade, it is possible to positively stir the processed product whose temperature has been increased by fermentation heat at the uppermost stage. In addition, the agitating blade having a lower inclination angle at the bottom stage can uniformly vent the entire processed product while reducing the applied load. As a result, it has high agitation performance, hardly causes poor fermentation, has few device failures and defective products (fermented compost), and shortens the processing time for drying and composting organic waste. Moreover, the amount of malodorous substances generated can be reduced by shortening the drying time.

  Further, the uppermost stirring blade has a width center line of the stirring blade that does not pass through the shaft center of the rotating shaft when viewed from the vertical upper side of the rotating shaft. Even when the inclination angle is large, the processed material spreads out evenly, and it is difficult to move toward the inner wall side of the container, thereby preventing poor fermentation and the like.

Since the waste treatment method of the present invention uses the above-described waste treatment apparatus of the present invention, poor fermentation is unlikely to occur, the processing time for drying and composting organic waste can be shortened, and the amount of malodorous substances generated is also reduced. it can. Further, the aeration amount is adjusted to 1/4 to 1/2 of the container volume (m ³ ) to perform aeration and agitation, and if necessary, the static pressure of the air supply means is set to 25 kPa or more. By heating the outside air sent from the means to 60 ° C. or higher, fermentation failure can be prevented, drying / composting treatment can be further shortened, and the amount of malodorous substances such as ammonia can be significantly reduced.

It is a longitudinal cross-sectional view which shows an example of the waste disposal apparatus of this invention. It is sectional drawing of the stirring blade in FIG. It is an enlarged view of the lowermost stirring blade in FIG. It is the schematic (no misalignment) which looked at the upper stage stirring blade from the perpendicular | vertical upper side of the rotating shaft, and the longitudinal cross-sectional view of a waste disposal apparatus. FIG. 2 is a schematic view (with misalignment) of an upper stirring blade as viewed from the vertical upper side of a rotation shaft, and a longitudinal sectional view of a waste disposal apparatus. It is a schematic diagram which shows the flow of the external air introduce | transduced in the container.

  An example of the waste treatment apparatus of the present invention will be described with reference to FIG. FIG. 1 is a longitudinal sectional view showing a configuration of a waste treatment apparatus. As shown in FIG. 1, the waste treatment apparatus 1 includes a cylindrical vertical container 2, a rotary shaft 3 provided in the vertical direction in the container 2, and a plurality of stirring blades fixed around the rotary shaft 3. 4 and a closed-type fermentation drying apparatus (component) including an air supply means 6 into the container 2. A vent hole 4d is provided at the lower part of the lowermost stirring blade, and outside air sent from the air feeding means 6 is introduced into the container through the pipe 6a provided in the rotating shaft. The container 2 that is a fermenter is a heat-insulating container having a metal outer layer and a heat insulating layer, and is an airtight container that is difficult to come into contact with outside air other than that introduced from a vent hole. The container 2 has an organic waste inlet 2a and a gas outlet 2c, and a compost (organic waste after treatment) outlet 2b at the bottom. The inlet 2a and the outlet 2b are provided with lids that can be opened and closed to ensure the hermeticity of the container.

  In the waste treatment apparatus of the present invention, the organic waste to be treated (hereinafter also simply referred to as “waste” or “treated product”) includes livestock excrement, food waste, septic tank sludge containing a large amount of organic components. Or mixtures thereof. Specific examples of livestock excrement include chicken dung, pig dung, cow dung, and horse dung. Food waste includes food waste and food production by-products. Examples include sludge extracted from a sludge septic tank. In addition, composting of waste is performed by aerobic fermentation while aeration is performed in the presence of aerobic fermentation bacteria in a container. As the aerobic fermenting bacteria, fermenting bacteria that are activated at about 30 to 90 ° C. are preferable, and examples thereof include Diovatisul and Bacillus.

  A machine room 5 is provided below the container 2, and a drive unit 8 for the rotating shaft 3 and the above-described air supply unit 6 are provided in the machine room. The rotating shaft 3 penetrates into the machine room 5 and is rotated at a predetermined number of rotations by the driving means 8. In addition, a heater 7 is provided for heating the outside air sent from the air supply means 6.

  In this apparatus, the processed product is input into the container 2 from the input port 2a, and the processed product is taken out from the outlet 2b at the bottom of the container after fermentation and composting in the container. Fermentation and composting are performed by rotating each stirring blade 4 at a low speed while introducing outside air from the vent holes 4d of the lowermost stirring blade, aeration and stirring the processed material, and aerobic fermentation. It is also dried simultaneously by ventilation. The outside air introduced into the container from the vent hole 4d of the lowermost stirring blade flows upward while passing through the processed material, and is exhausted from the exhaust port 2c together with the gas and water vapor generated from the processed material. This exhaust is forcibly performed by an exhaust blower (not shown) connected to the exhaust port 2c.

  A predetermined number of stirring blades 4 are provided in each stage at a plurality of positions spaced apart from each other by a predetermined interval from the lower part to the upper part of the rotating shaft 3 in the container. In the form shown in FIG. 1, the number of stages is five, and the number of stirring blades is three in the first stage from the bottom (one is not shown), two in the second stage, and one in the third stage. A total of 9 sheets are provided, one on the fourth level and two on the fifth level. The number of stages of the stirring blade 4 is not limited to the example shown in FIG. 1, and it is preferable to provide at least three stages or more. In FIG. 1, the first stage from the bottom is classified as “lower stage”, the second stage and third stage as “middle stage”, and the fourth stage and fifth stage as “upper stage”. Here, when the number of stages is three or more and an arbitrary number of stages, the uppermost stage is always classified as “upper stage”, and the lowermost stage is always classified as “lower stage”. With respect to other than the uppermost and lowermost stages, at least one stage is set as “middle stage”, and the rest is classified into “upper stage”, “middle stage”, and “lower stage” according to the position. The “upper stage” is in an area above the vertical center position of the container 2, and the “lower stage” is in an area below the vertical center position of the container 2.

  Further, the number of stirring blades in each stage is not limited to the example shown in FIG. 1, and at least one stirring blade may be provided. About the lowermost stirring blade (with a vent hole), it is preferable to provide three or more at regular intervals in the circumferential direction in order to uniformly and sufficiently ventilate the whole. Note that the load applied to the stirring blade increases from the upper stage to the lower stage, and in each stirring blade, the load applied to the part closer to the main shaft decreases.

  As will be described later, the waste (processed material) is not filled in the container 2 and is charged with a space of about 10 to 20%. The stirring blade 4 is disposed in a range from the bottom of the container 2 to the height H of the processed object, and the position of the uppermost stirring blade is positioned at the substantially uppermost part of the processed object. The position of the lowermost stirring blade is preferably slightly above the bottom of the container 2 and a gap is preferably provided between the bottom. In addition, the distance between each stage can be arbitrarily determined according to the number of stages with reference to the uppermost stage and the lowermost stage.

  In some conventional closed-type fermentative drying apparatuses, the stirring blades are provided in a plurality of stages. However, it is recognized that the stirring blades are only used for stirring (the bottom stage is also vented), and all the stages are used. The same shape of the impeller is used, and the role of each stage has not been sufficiently studied. On the other hand, in the present invention, the role of the stirring blade is clarified in each stage (particularly, the three stages of the lower stage, the middle stage, and the upper stage), and the form thereof is examined based on this.

  Each role is as follows. The upper stage is used to promote fermentation by flattening the treated product and increasing the contact area with the outside air (aerated from the stirring blade). The middle stage is used to actively agitate the processed product whose temperature has been increased by fermentation heat in the upper stage. The lower stage (particularly the lowermost stage) is mainly used for aeration because the stirring is completed in the upper stage and the middle stage.

  All the stirring blades 4 have a pitched paddle shape linearly extending from the rotary shaft 3 toward the inner wall side of the container 2 and have an inclined surface on the front side in the rotation direction. The inclined surfaces of the stirring blades 4 are planes inclined at an inclination angle of less than 90 degrees (acute angle) with respect to the rotation surface (horizontal plane) of the stirring blades. That is, the angle formed between the rear direction in the rotation direction and the upper direction of the inclined surface is less than 90 degrees. As the agitating blade rotates, the processed material is agitated in such a manner as to run along the inclined surface.

  The shape of the stirring blade will be described in detail with reference to FIG. FIG. 2 is a cross-sectional view in the direction of the rotation axis of the stirring blade at each stage in FIG. As shown in FIG. 2, each stirring blade 4 is joined to the bottom plate 4b parallel (horizontal) to the rotation surface of the stirring blade, the swash plate 4a joined to the bottom plate 4b, and the bottom plate 4b and the swash plate 4a. And a bent plate 4c having an L-shaped cross section. The outer surface (planar surface) of the swash plate 4a is the above-mentioned “inclined surface of the stirring blade”, and the swash plate 4a is joined to the front side in the rotational direction of the bottom plate 4b. In addition, as long as the shape of the stirring blade has the above-described inclined surface, the other specific structure is not particularly limited to the shape shown in FIG. However, for the lowermost stirring blade, the outside air path described later is required.

In the waste treatment apparatus of the present invention, the inclination angle θ ₁ of the inclined surface of the upper (including the uppermost) stirring blade 4 is equal to the inclination angle θ ₃ of the inclined surface of the lower (including the lowermost) stirring blade 4. 2 times or more. About an upper stage, it becomes easy to extend a processed material flatly by making an inclination | tilt angle high, and can increase the contact area with external air. Moreover, since it is an upper part of a processed material, stirring resistance is small and a load is hard to become large even at a high inclination angle. On the other hand, the lower stage has a large stirring resistance because it is the lower part of the processed product, but the load can be reduced by lowering the inclination angle (less than 1/2 of the uppermost stage). Further, since the stirring is completed in the upper stage and the middle stage, even if the inclination angle is lowered and the stirring performance of the portion is lowered, sufficient stirring performance can be exhibited as the entire apparatus. Furthermore, the inclination angle of the lowermost stirring blade does not adversely affect the aeration performance which is the role of the stirring blade.

The inclination angle θ ₂ of the inclined surface of the middle stirring blade 4 is equal to or greater than the inclination angle θ ₃ of the inclined surface of the lower stirring blade 4 (including the lowermost) stirring blade, and the upper stirring blade (including the uppermost stirring blade). 4 is the inclination angle theta ₁ following the inclined surface of the. That is, θ ₃ ≦ θ ₂ ≦ θ ₁ is satisfied. In order to secure the stirring performance while reducing the load applied to the stirring blade, θ ₂ is preferably set to θ ₃ <θ ₂ <θ ₁ . The middle stage is used to actively agitate the processed product whose temperature has been increased by fermentation heat in the upper stage. In the middle stage, if there is a lot of downward flow, it will lead to a decrease in the contact time and the amount of contact with the outside air, but by using a stirring blade having the above inclination angle, this downward flow is minimized. Can do. In addition, the larger the middle inclination angle, the better the stirring performance, but the greater the load.

Specific inclination angle, upper inclination angle theta ₁ of the inclined surface of the stirring blade 4 (uppermost including) is preferably 45 to 75 degrees, more preferably 55 to 75 degrees, 60 degrees to 70 degrees Is more preferable, and 62 to 67 degrees is particularly preferable. The inclination angle θ ₃ of the inclined surface of the lower (including the lowermost) stirring blade 4 is preferably 10 to 30 degrees, more preferably 15 to 25 degrees, and particularly preferably 18 to 22 degrees. In selecting the tilt angle, θ ₁ ≧ θ ₃ × 2 is satisfied in any case. The inclination angle θ ₂ of the inclined surface of the middle stirring blade 4 is preferably 25 to 75 degrees, more preferably 25 to 65 degrees, further preferably 25 to 55 degrees, and particularly preferably 25 to 45 degrees. In consideration of the stirring performance and the load applied to the stirring blade, it is most preferable that θ ₁ = 65 degrees, θ ₂ = 32 degrees, and θ ₃ = 20 degrees in the configuration shown in FIG. 1 (all five stages).

  Each stirring blade 4 has a hollow portion 4e surrounded by a swash plate 4a, a bottom plate 4b, and a bent plate 4c. The hollow portion 4e of the lowermost stirring blade 4 communicates with the pipe 6a (see FIG. 1) in the rotating shaft 3 to form an outside air path to the vent hole 4d (through hole) provided in the lower part of the bent plate 4c. doing. Since the lower part of the bent plate 4c provided with the vent hole 4d is located on the rear side in the rotational direction, clogging due to the processed material is unlikely to occur. In the embodiment shown in FIG. 1, the vent hole is formed only in the lowermost stirring blade. However, the present invention is not limited to this. For example, the vent hole may be formed in the further stirring blade. .

  Also, as shown in FIG. 3, a plurality of vent holes 4d are provided in the longitudinal direction of the stirring blade 4, and the intervals are closer in steps toward the outer side in the longitudinal direction of the stirring blade (inner wall side of the container). It is formed to become. By arranging the vent hole 4d in this way, when taking out the compost from the take-out port 2b (see FIG. 1) provided near the inner wall side of the container 2, it can be taken out in a sufficiently ventilated and dried state. it can.

  4 (a) and 5 (a) are schematic views of the uppermost stirring blade as viewed from the vertical upper side of the rotation axis. FIG. 4A shows a case where the stirring blade is provided without misalignment, and FIG. 5A shows a case where the stirring blade is provided with misalignment. In each figure, the black arrow in the figure is the direction of rotation of the stirring blade. In the form shown in FIG. 4A, when the upper stirring blade 4 is fixed to the rotating shaft 3, the center line of the width of the stirring blade (dotted line in the figure) passes through the shaft core 3a of the rotating shaft 3. It is provided without deviation. This is a normal form in a general closed fermentation drying apparatus. In this case, if the inclination angle of the upper stirring blade is too large, the processed material spreads outward and tends to be closer to the inner wall side of the container 2 (dotted line arrow in the figure). Thereby, as shown in FIG.4 (b), the processed material which approached the outside becomes easy to move to the lower part along the inner wall of the container 2. FIG. As a result, the upper part of the processed product cannot be flattened, the contact area with the aeration is reduced, and the contact time with the aeration is shortened because it moves to the lower part along the inner wall, so that fermentation may not be sufficiently performed. is there.

  On the other hand, in the form shown in FIG. 5A, when the upper stirring blade 4 is fixed to the rotary shaft 3, the width center line (dotted line in the figure) of the stirring blade does not pass through the shaft core 3 a of the rotary shaft 3. So that the core is shifted. In this case, even when the inclination angle of the upper stirring blade is large, the processed material spreads out evenly and hardly moves toward the inner wall side of the container 2 (dotted arrow in the figure). For this reason, as shown in FIG.5 (b), the phenomenon that the processed material which moved to the outer side moves below along the inner wall of the container 2 does not occur, and fermentation can fully be performed.

  In the present invention, either of the configurations shown in FIGS. 4A and 5A can be adopted, but the inclination angle of the upper stirring blade is set higher than that in a general closed-type fermentation drying apparatus. Therefore, as shown in FIG. 5 (a) in particular, it is preferable to provide it with misalignment. The deviation width between the rotation direction width center line of the stirring blade and the axis of the rotation shaft is about 2 to 60% of the rotation shaft diameter.

  The waste treatment method of the present invention is characterized in that organic waste is composted using the above-described waste treatment apparatus of the present invention. The specific processing procedure is as follows.

(1) First, waste (processed material) is thrown into the waste treatment apparatus leaving a space of 10 to 20% with respect to the internal volume of the apparatus. By adding the processed product while leaving a space of 10 to 20%, the processed product is sufficiently stirred, so that fermentation and drying are efficiently performed.

(2) The treated product is fermented and dried under predetermined conditions.
There are two operation methods, “batch operation” and “continuous operation”.
(A) In the case of “batch operation”, the treated product is put into a waste treatment apparatus, the stirring blade is rotated at a low speed, and is fermented and dried for about 5 days while being aerated through the vent hole of the lowermost stirring blade. . There will be no removal or loading for the last 5 days. Thereafter, about 30% by mass of fermented and dried processed material (compost) is left in the apparatus, and the remaining 70% by mass of compost is taken out. The extracted compost becomes the product. If necessary, this may be granulated. The compost left in the waste treatment apparatus is fermented and dried for about 5 days to be composted while being stirred under the same conditions as the previous one together with the newly added treatment.
(B) In the case of “continuous operation”, the treated product is put into a waste treatment apparatus, fermented and dried for 24 hours, and about 20% by mass of compost is taken out 24 hours after the start of operation. After that, a new processed product for the taken-out amount is charged. In this way, treatment input and compost removal are repeated in a 24-hour cycle.

  In any case, when the waste treatment apparatus is used for the first time, it is preferable to add in advance about 30% by mass of the previous compost that has been fermented and taken out from this apparatus. This is because acclimated fermentative bacteria are used.

  In any operation, the rotation speed of the stirring blade is adjusted by the moisture content of the processed product, and specifically, the moisture content is adjusted to be less than 35%. Usually, the number of rotations is adjusted so as to rotate once in 40 to 60 minutes. The moisture content of the treated product also depends on the rotation speed of the stirring blade, and there is a possibility that the moisture content will be 35% or more in either case of being too early or too late. Moreover, when the moisture content is 35% or more, it may be difficult to remove from the container.

In any operation, the air flow rate per minute (m ³ ) introduced into the container is set to about 1/8 to 1 of the container internal volume (m ³ ). Aeration is continued during the treatment period. Since the drying time can be shortened and the amount of malodorous substances generated can be reduced, it is preferable to positively increase the air flow rate in the present invention. Specifically, the air flow rate is generally about 1/8 to 1/6 of the inner volume (m ³ ) of the container. In the present invention, the air flow rate is set to a range of 1/4 to 1/2. It is preferable to do. That is, for example, when the container volume is 36 m ³ , the ventilation rate is preferably 9 to 18 m ³ / min.

  When the amount of ventilation is small, as shown in FIG. 6 (a), the flow of outside air introduced from the ventilation holes 4d of the lowermost stirring blade 4 (arrow in the figure) is biased toward the inner wall side of the container 2 and rotates. The ventilation on the shaft 3 side may not be sufficient. This is not preferable because it leads to poor fermentation in the portion on the rotating shaft side. Moreover, even if the air flow rate is simply increased, depending on the mode of the air supply means, the flow of outside air may be biased to the outside, resulting in a decrease in temperature at this portion, which may result in poor fermentation. In the case where the processing time is prioritized over the operation cost, the temperature drop can be coped with by heating and introducing the outside air with the heater 7. When heating the outside air to introduce | transducing, it is preferable to set it as 60 degreeC or more from the relationship with an aerobic fermentation microbe.

The medium-pressure blower (air supply means) that has been generally used from the past has a static pressure of 10 to 15 kPa, and the ventilation rate is ¼ of the above preferred range (the inner volume (m ³ ) of the container). ~ 1/2) is difficult. Moreover, even if the air flow rate can be increased, there is a risk of the above-mentioned bias. Therefore, in order to the aeration the preferred range (1 / 4-1 / 2 of the internal volume of the vessel ^{(m 3))} may be used high pressure blower (air supply means) static pressure is greater than or equal to 25kPa Is preferred. By using such a high-pressure blower, as shown in FIG. 6 (b), a sufficient amount of ventilation can be ensured in the entire container 2, and the ventilation on the rotating shaft 3 side is sufficiently performed. The bias to the side can be prevented.

  Using a small experimental machine simulating the waste treatment apparatus of the present invention shown in FIG. 1, the effect of the difference in the shape of the stirring blade was verified. This is shown below.

Reference Example 1 to Reference Example 5
As shown in FIG. 1, a total of nine agitating blades in five stages around the rotation axis are installed in the center of a cylindrical vessel having a bottom surface diameter of 190 mm and an internal volume of 3.6 L. Fixed. Steps with two or more stirring blades were provided at equal intervals in the circumferential direction. The mode of the stirring blade (inclined surface angle and presence / absence of misalignment) is as shown in Table 1. The shaft diameter of the rotating shaft is 12 mm, the width in the rotating direction of the stirring blade is 9 mm, and the length in the longitudinal direction is 85 mm. “Center misalignment” in Table 1 was fixed when the stirring blade was viewed from the vertical upper side of the rotating shaft and the width center line of the stirring blade was shifted by 6.5 mm from the axial center of the rotating shaft. Water was put in this container to a position where the uppermost stirring blade was immersed, and a small experimental machine simulating the waste treatment apparatus of the present invention was obtained. Reference Examples 1 to 4 in Table 1 are examples corresponding to the stirring blades of the waste treatment apparatus of the present invention, and Reference Example 5 is an example corresponding to the stirring blades of the conventional waste treatment apparatus.

  Using this small experimental machine, the rotation speed of the rotating shaft was adjusted to 0.2 minutes per rotation and rotated, and ink was introduced from the upper stage (water surface) and middle stage (water level center), and after 3 minutes had passed. The state of the ink diffusion was photographed from a plurality of directions, and the colored area and volume were calculated from there. In addition, since stirring performance cannot be evaluated accurately only with this area and volume, the result of visual observation during the test is shown in the column of “Effect” in Table 1. The load in Table 1 was calculated as a relative value with respect to the required power for stirring, with Reference Example 5 being 100%. The results are also shown in Table 1.

  As shown in Table 1, when the inclination angle of the stirring blade is increased, the stirring / mixing ability is increased, but when an uneven flow occurs, a downward flow is generated. Therefore, it can be said that the upper stirrer blade preferably has a shape that does not flow downward and can further expand the processed material, and the middle step preferably has a shape with higher stirring performance.

Reference Example 6 and Reference Example 7
Raw swine dung was used as a raw material, and the malodor reduction effect was verified using the waste disposal apparatus (S36) shown in FIG. 1 having an internal volume of 36 m ³ . The apparatus configuration is as shown in FIG. A total of nine stirring blades were fixed in five stages around the rotation axis, and two or more stages were provided at equal intervals in the circumferential direction. The inclined surface angles of the stirring blades were θ ₁ = 65 degrees, θ ₂ = 40 degrees, θ ₃ = 25 degrees, the width in the rotational direction was 190 mm, the length in the longitudinal direction was 1900 mm, and there was no misalignment. The rotation of the stirring blade was adjusted to 40 to 60 minutes per rotation, and aeration was continuously performed for 14 days with a predetermined aeration amount. Specifically, in Reference Example 6, the air flow rate was 12 m ³ / min (static pressure of the air blower of 25 kPa or more) and heated to 70 ° C., and in Reference Example 7, the air flow rate was 6 m ³ / min (of the air blower). The static pressure is 10 to 15 kPa) and is not heated (the outside air temperature during the test is 15 ° C. on average).

  Table 2 shows test conditions and measurement results such as total nitrogen. In Table 2, the loss on ignition is a value measured by the 3.2.1 ignition ashing method of the fertilizer analysis method (Agricultural and Environmental Technology Research Institute, Ministry of Agriculture, Forestry and Fisheries, 1992). Reference examples 6 and 7 in the item of raw materials are analysis values of the product before the test, respectively. The input amount represents the weight of pig manure processed per day. Moisture indicates the moisture content. The loss on ignition indicates the ratio of the amount of organic matter and serves as an index representing the decomposition of the organic matter. Total nitrogen is the amount of nitrogen, and (dry matter)% is the amount of nitrogen when the raw material or each treated product has a moisture content of 0%. Further, (weight) and (volume) specify the weight and volume of nitrogen, respectively. The C / N ratio represents the ratio of each carbon and nitrogen.

In Reference Example 7 (aeration amount: normal) and Reference Example 6 (aeration amount: twice the normal amount), there is a difference of about 1% in the total nitrogen. When this is numerically analyzed, the amount of nitrogen released in the raw material by the treatment of Reference Example 6 is (80.6-76.8) = 3.8 m ³ . The amount of nitrogen released in the raw material by the treatment of Reference Example 7 is (35.3-26.1) = 9.2 m ³ , and the input amount of Reference Example 6 is 2.29 times the input amount of Reference Example 7. Nevertheless, it can be seen that the release amount of nitrogen in the raw material is greatly reduced to 41.3% (about 18%, which is a release amount of 21.1 mm ^{3 in} volume ratio). Therefore, in this test, it can be said that the release amount of nitrogenous malodorous substances such as ammonia was reduced by about 82%. The ammonia concentration discharged from the exhaust port was reduced to 350 ppm in Reference Example 6 as compared to 900 ppm in Reference Example 7.

  One of the major factors is the amount of input per hour (processing amount), which is [24h / 3500kg] to [24h / 8000kg], that is, 0.41min / kg to 0.18min / kg. The time is shortened by 44%. Since the nitrogenous malodorous substance dissolves in water and is released, it can be said that the time to dissolve is 44%. Inferring from the viewpoint of time, it can be said that the amount of release decreased as the “melting time” was shortened. The compost product of Reference Example 6 is quite effective as a fertilizer because the amount of nitrogen is as high as 4.43%, and the decrease in ignition loss is about 15% and has an appropriate organic matter. It is guessed.

  The waste treatment apparatus of the present invention has high agitation performance, is less prone to fermentation, can reduce the processing time of drying and composting of organic waste, and can reduce the generation amount of malodorous substances. It can be suitably used as a closed fermentation drying apparatus (component) for composting organic waste such as livestock excreta discharged from the body and food residues discharged from food industry establishments.

DESCRIPTION OF SYMBOLS 1 Waste disposal apparatus 2 Container 3 Rotating shaft 4 Stirring blade 5 Machine room 6 Air supply means 7 Heater 8 Drive means

Claims (6)

An airtight vertical container, a rotary shaft provided in the vertical direction in the container, a plurality of stirring blades fixed around the rotary shaft, and an air supply means for sending outside air into the container A waste treatment apparatus for removing organic waste introduced from the upper part of the container into the container by fermenting and drying the agitation with the stirring blade, composting and composting the organic waste. ,
The agitating blades are spaced apart at a predetermined interval from the lower part to the upper part of the rotating shaft in the container, at least at least three stages, and at least one sheet at each stage, from the rotating shaft toward the inner wall of the container. It extends in a straight line,
The lowermost stirring blade is connected to the air supply means, and has a vent hole for introducing outside air sent from the air supply means into the container,
The stirring blade has an inclined surface on the front side in the rotation direction,
An inclination angle of the inclined surface of the uppermost stirring blade with respect to the rotating surface of the stirring blade is less than 90 degrees, and an inclination angle of the inclined surface of the lowermost stirring blade with respect to the rotating surface of the stirring blade is 2 More than double
The inclination angle of the stirring blades other than the uppermost stage and the lowermost stage with respect to the rotation surface of the stirring blade is equal to or greater than the inclination angle of the lowermost stirring blade with respect to the rotation surface of the stirring blade. der inclination angle less with respect to the rotation plane of the stirring blade in the inclined surface of the stirring blade is,
The uppermost stirring blade has an inclination angle of 55 to 75 degrees with respect to the rotation surface of the stirring blade at the inclined surface, and the width center line of the stirring blade when viewed from the vertical upper side of the rotation shaft. Does not pass through the axis of the rotating shaft .   The inclination angle of the uppermost stirring blade with respect to the rotation surface of the stirring blade is 55 ° to 65 °, and the inclination angle of the lowermost stirring blade with respect to the rotation surface of the stirring blade is 15 °. The waste disposal apparatus according to claim 1, wherein the waste disposal apparatus is -25 degrees. A waste treatment method for composting organic waste using a waste treatment device,
The waste treatment apparatus according to claim 1 or 2 , wherein the waste treatment apparatus is the waste treatment apparatus according to claim 1 or 2 . In the waste treatment apparatus, the aeration amount (m ³ ) per minute introduced into the container by the air feeding means is adjusted to ¼ to ½ of the inner volume (m ³ ) of the container. 4. The waste treatment method according to claim 3, wherein aeration and agitation are performed. 5. The waste treatment method according to claim 4 , wherein in the waste treatment apparatus, the static pressure of the air supply means is 25 kPa or more. The waste treatment method according to claim 4 or 5, wherein in the waste treatment apparatus, the outside air sent from the air feeding means is heated to 60 ° C or more and introduced into the container.

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