JP2539728B2 - Method and apparatus for promoting fermentation of organic sludge using an inclined surface - Google Patents

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for promoting fermentation of organic sludge using an inclined surface,
Even if the fermentation process is carried out by a fermentation machine, it is possible to repeatedly perform natural air-ration (mixing or cutting back to expose the fermentation product to the air) to the fermentation product that is incomplete in moisture adjustment and immature. By further increasing the fermentation efficiency by, and by packing the primary fermentation product in a bag with good air permeability in a predetermined volume for a certain period of time, a further fermented secondary fermentation product was obtained. The purpose is to

[0002]

2. Description of the Related Art The applicant of the present application previously provided a recycling greening method called a PMC method (see Japanese Patent Publication No. 4-45613 and Japanese Patent Application Laid-Open No. 4-261914). That P
The MC method is an organic growth base that is produced by mixing compost of public sewage sludge or livestock manure and charcoal powder, or incineration ash generated from various industries such as incineration ash of pulp slag produced during pulp manufacturing and fermentation. A method of producing a growth base of plants in a revegetation work by producing a wood and using this growth base material and an adhesive material called "P-MZAI (registered trademark)" which mainly uses konjak flying powder. is there.

[0003]

The above-mentioned PMC method substitutes black soil and mountain sand used as a vegetation base material in the conventional method, and also contains a large amount of fertilizer. Furthermore, it is useful as a modern construction method that prevents the destruction of nature by collecting sand and recycles waste. On the other hand, in the above-mentioned PMC method, in order to promote the fermentation of organic substances, the failure of adjusting the water content affects the period of completion of the fermentation. In the conventional method of the applicant of the present application, when the water content of the organic sludge is poorly adjusted by using a kiln type (horizontal type) fermentation machine,
Poor and unripe compost with a large amount of water discharged from the fermentation machine needs to be adjusted again. However, in the conventional method, in order to adjust the water content of the unripened fermented material again, it is put into the fermenting machine again for fermentation, or it is accumulated for a long time, and the unripened fermented material is manually or through a device. No more effective and appropriate method could be found other than repeating the aeration.

[0004]

Therefore, the present invention is provided to solve the problems of the prior art publications and to achieve the object of the invention. That is, a first aspect of the present invention is a method for promoting fermentation of an organic sludge using an inclined surface, wherein a mixture of incinerated ash of pulp slag is mixed with sewage sludge in a substantially equal ratio to appropriately deodorize and ferment the mixture. The primary fermented substance discharged from the discharge port of the fermentation machine was charged into the machine and the mixture was transferred with stirring by rotating the body of the fermentation machine and heated air by the burner was supplied so as to contact the surface of the mixture. Is continuously dropped to the lower inclined surface, the primary fermentation product with good water content is slid down on the inclined surface and deposited at the lower end deposition position, and the primary fermentation product with a large amount of water that is poorly adjusted is on the inclined surface. and temporarily stay on the inclined surface by its own weight, including moisture for the angle, intensified fermentation by the outside air infiltrated contacted in the dwell position, the inclined surface of the primary fermentation product that accumulated on the inclined surface moisture is reduced by the passage of time It is obtained so as to slide down fall deposition position of the edge.

A second aspect of the present invention is an apparatus for promoting fermentation of organic sludge using an inclined surface, which is a kiln type fermentation machine having a mixture inlet at one end and an outlet at the other end,
Below the discharge port of the fermentation machine, when the fermented product that has been fermented and discharged with good water content adjustment falls, it will slide to the lower end of the inclined surface, and if the immature fermented material with poor water content adjustment falls, the water content will drop. Including 30 to 60 degrees that temporarily stays under its own weight
The angle forming a sloping surface to variable is and what is water adjusted to a lower end position of the inclined surface to form a deposition field to be deposited slides down falling good primary fermentation product.

A third aspect of the present invention is a method for promoting fermentation of an organic sludge using an inclined surface according to the first aspect of the invention, wherein the primary fermented material that has reached the sedimentation site is set to have a large capacity for the outside air to pass through. Then, it is packaged in a bag, stored for a predetermined period of time, and then subjected to secondary fermentation.

[0007]

[Operation] The sewage sludge is unloaded from the sludge carrier to the prescribed mixing treatment plant, and then the incineration ash of the valp slag having carbonized charcoal fiber and having a heat of about 40 to 60 ° C. and 50% of the sewage sludge
Add and mix at a rate of one at a time. As a result, the temperature of the combustion ash of pulp slag decreases due to the heat exchange action, but the moisture of the sludge is adjusted to promote fermentation, and the malodor generated from the sewage sludge causes a considerable deodorizing action when mixed with the combustion ash. . Next, the mixture having the water content adjusted and deodorized is charged from the charging port at one end of the kiln type fermentation machine, and heated air is supplied to the surface of the mixture by a burner in the fermentation machine, By rotating the body of the fermentation machine, the mixture is stirred and transferred to perform fermentation and deodorization, and the primary fermentation product is discharged from the discharge port and dropped onto the inclined surface. On this slope, the primary fermented product with a good water content slides down and is deposited on the bottom of the slope. And, the primary fermentation product which is not matured due to poor moisture control is temporarily retained on the inclined surface, but considerable heat is retained even at the retention point, and the fermentation is continued by permeation of the outside air, and the moisture regulation is in a good state. Then, it starts to slide down and slides down to the deposit area at the bottom of the slope. Then, by setting this to a large volume that allows the outside air to permeate the bag with good air permeability, bag it, and store it for 1 to 3 months, the secondary fermentation will naturally start and it will mature completely. The secondary fermented product is obtained, and an almost odorless, dark soil-like growth base material is produced.

[0008]

Embodiments of the present invention will now be described with reference to the drawings.
1 is a schematic side view showing a fermentation promoting process of organic sludge using an inclined surface according to the present invention, FIG. 2 is a front view of a fermentation machine for carrying out a fermentation promoting method of sewage sludge, and FIG. 3 is a plan view of FIG. ,
FIG. 4 is a sectional view taken along line 4-4 of FIG. In the figure, reference numeral 1 denotes a rotary drum fermentation machine 2 mixture M introduced chamber consisting of ash 1 ₂ sewage sludge 1 ₁ and pulp debris -, 3 the discharge chamber of the primary fermentation product -, 4 through the heated air It is a chamber, and a kiln-type fermentation machine A is constructed by using these as main elements. The fermentation machine A is installed on a base surface B, and the rotary drum 1 is connected and supported by a mixture input chamber-2 and a discharge chamber-3. The rotary drum 1 is rotatably supported by a pair of left and right rollers 5 installed on the base surface B. The hot-air penetration chamber 4 is fixedly supported by the mixture input chamber-2 and the discharge chamber-3 in the axial direction of the rotary drum 1. In addition, the rotary drum 1 described above
Is provided with a drive chain 9 on its outer periphery, and a sprocket 6 driven by a motor 7 is meshed with the drive chain 9. Reference numeral 11 denotes a plurality of feed blades provided on the inner peripheral surface of the rotary drum 1. The feed blades 11 are spirally projecting in directions opposite to each other with respect to the axis, and the feed blades are inclined to feed to the discharge chamber-3 side. There is. The outer periphery of the rotary drum 1 is covered with a heat insulating material 8. Reference numeral 12 denotes an arm-shaped intake / exhaust pipe provided so as to communicate with the hot air penetration chamber 4 in the rotary drum 1, and the inlet / outlet 12 ₁ at the tip thereof is installed toward the outlet 22. Reference numeral 13 denotes a stirring arm provided in the hot air penetration chamber-4 like the intake / exhaust pipe 12, but the arm itself is pure and is not in communication with the chamber. The charging chamber-2 is equipped with a hopper-10 from which the mixture is charged into the drum. A duct 14 is connected to the end of the hot air penetration chamber-4 in the charging chamber-2, and a damper is provided in the middle thereof.
15 are provided. The discharge chamber-3 is provided with a burner 18 and a temperature sensor-19, and a blower fan 21 is attached as necessary to always send fresh hot air to the rotary drum 1. The discharge chamber is provided with a discharge port 22 for discharging the primary fermentation product M ′ which transfers the mixture M which is starting fermentation in the drum while stirring. Reference numeral 24 denotes a downwardly sloping inclined surface formed below the discharge port 22 of the fermentation machine. Specifically, the inclination angle θ is set to 30 to 60 degrees, the width is set to about 5 m, and the length is set to about 15 m. When the discharge port and the inclined surface are separated, a belt conveyor is arranged to convey the primary fermentation product. 25 is the primary fermentation product M'formed at the lower end of the inclined surface
And 26 is a secondary fermentation deposition site for further fermenting the primary fermentation product, and the deposition site is to be installed if necessary. Reference numeral 27 is a belt conveyor, and 28 is a bag having good air permeability for packing the primary fermentation product M ′ that has fallen from the inclined surface 24 to the deposition site.
In order to have a large volume that allows the outside air to permeate inside the fermented product, it is set to 1 cubic meter per bag. In addition, the primary fermentation product M ′ may be temporarily accumulated in the accumulation field at the lower end of the inclined surface if necessary, and the secondary fermentation may be started before being packed in the bag 28. Reference numeral 29 is a storage space for stacking the packed bag bodies 28 in multiple stages via a cage or a wooden lattice 30.

[0009]

11. Specific steps example sewage sludge treatment plant, collecting loading to unloading the sewage sludge 1 ₁ fetid that has carried in the sludge truck in a predetermined mixing treatment plants G, Shoberuka - charcoal fiber through carbonization If the was 40 to 50 ° C approximately pulp slag ash 1 ₂ adding and mixing at a rate of the sewage sludge and 50% increments, the combustion ash 1 ₂ the temperature is lowered by heat exchange action, sewage sludge 1 ₁ moisture encourage adjusted to fermentation, deodorization is effected malodors and generated from the sewage sludge in considerable under the action of combustion ash 1 _2. In this case, the sufficiently mixed mixture M has a water content ratio of 60% and a temperature of about 30 ° C. The malodor generated from sewage sludge by combustion ash 1 ₂ pulp dregs are considerably deodorized. Next, the above mixture is charged from the charging hopper 10 at one end of the kiln type fermentation machine A, the heating air by the burner 18 is supplied into the rotary drum 1 in the fermentation machine, and the heating air is mixed. The composted primary fermentation product is discharged from the discharge port 22 while contacting the surface of M and rotating and rotating the drum 1 of the fermentation machine to agitate and transfer the mixture M to promote fermentation and deodorization. The discharged primary fermentation product M ′ has a water content ratio of 50.
%, And a temperature of about 50 ° C. to 60 ° C. is set as an appropriate value. The discharged primary fermented material M ′ drops onto the sloped surface 24 having a downward slope, and the primary fermented material having a proper water content ratio and good water content on the sloped surface slides down the sloped surface and is deposited at the lower end of the deposition field 25. Be deposited on. And, in the primary fermented product, a portion with a high water content and a water content ratio of more than 50% stays on the inclined surface when it falls on the inclined surface. Fermentation is promoted due to the permeation of water and the water content is adjusted to a good state, the sliding starts again and the water falls to the deposition site 25. The primary fermentation product M deposited on the deposition site 25 is packed in a breathable bag 28 as it is using the shoveler-S and the conveyor 27, and then stored for a certain period of time to carry out secondary fermentation in the bag. Fermentation is promoted without artificial aeration, resulting in a better-aged secondary fermentation product M ″.
The primary fermentation product M ′ deposited on the sedimentation site may be transferred to another secondary fermentation sedimentation site 26 and piled up in a height of about 1.5 to 2.0 m. As a result, the temperature of about 40 to 60 ° C rises from the surface of the fermented material piled up in the field to the thickness t of about 50 to 80 cm, and the secondary fermentation begins to ripen. Then, the aged portion of the secondary fermented matter M ″ which has been piled up is conveyed by the belt conveyor 27 to be filled in a bag 28 having good air permeability. The filled bag 28 is stored in the storage room 29 in a cage or a wooden lattice. It is stacked and stored in a plurality of stages via 30. During the storage, the secondary fermentation product M ″ in the bag body promotes fermentation without air-ration. The pile of piles of the scraped secondary fermentation product M ″ has a better air permeability up to a thickness of 50 to 80 cm from the surface thereof, so that the secondary fermentation is further activated.

[0010]

EFFECTS OF THE INVENTION Since the present invention has the above-mentioned constitution, in claims 1 and 2, even if the fermentation treatment is carried out by a fermentation machine, the water content is insufficient and the unripened primary fermentation product is specified. By dropping it on the inclined surface of the angle, it is possible to repeat the natural aeration on the inclined surface without human intervention, which makes it possible to adjust the water content sufficiently and increase the fermentation efficiency, and to ensure uniform quality growth. A base material can be produced. Further, according to claim 3, the fermented product having undergone the secondary fermentation is packed in a bag having good air permeability and stored for a predetermined period of time, thereby saving an air ratio which requires manpower. You can And that air
By omitting the ratio, dispersion of the fermentation heat can be prevented. In addition, the bag used for bagging has a diameter of 1 m or less and accommodates a relatively large volume of secondary fermented product of about 1 cubic m per bag, so that the outside air can penetrate to the vicinity of the center of the bag. The fermentation can be further promoted.

[Brief description of drawings]

FIG. 1 is a schematic side view showing a process of promoting fermentation of organic sludge using an inclined surface according to the present invention.

FIG. 2 is a front view of a fermentation machine for a mixture.

FIG. 3 is a plan view of FIG.

4 is a cross-sectional view taken along line 4-4 of FIG.

[Explanation of symbols]

 1 Rotating Drum 2 Charge Chamber-3 Discharging Chamber-4 Hot Air Penetration Chamber-5 Rotating Drum Support Roller 6 Sprocket 7 Motor with Reducer 8 Insulation 9 Drive Chain 10 Hopper 11 Feeding Blade 12 Arm type intake / exhaust pipe 13 Stirring arm 14 Duct on the side of the charging chamber 15 Duct damper 17 Inspection port 18 Burner 19 Temperature sensor-20 Damper 21 Blower fan 22 Discharge port 24 Down slope 25 Primary fermentation deposits 26 Secondary fermentation deposits 27 Belt conveyor 28 Bags

Claims (3)

(57) [Claims] 1. A sewage sludge is mixed with incinerated ash of pulp slag at a substantially equal ratio, and the mixture is appropriately deodorized and the water content is adjusted, and the mixture is put into a fermentation machine. The mixture is agitated by rotating the body of the fermentation machine. While being transferred, the heated air from the burner is supplied so as to come into contact with the surface of the mixture, and the primary fermentation product discharged from the discharge port of the fermentation machine is continuously dropped onto the lower inclined surface, and the water content is adjusted on the inclined surface. by sliding down the good primary fermentation was deposited in the deposition position of the lower end, the primary fermentation of misalignment are much moisture the moisture with respect to the angle of the inclined surface
Temporarily stays on the inclined surface by its own weight, activates fermentation by permeating external air at the staying position, and the primary fermentation product retained on the inclined surface whose water content has decreased over time is accumulated at the lower end of the inclined surface. A method for accelerating the fermentation of organic sludge using an inclined surface, which is characterized in that it slid down onto the surface. 2. A kiln-type fermentation machine having a mixture inlet at one end and a discharge outlet at the other end, in the lower part of the outlet of the fermentation machine, the primary water content of the fermented product is adjusted and discharged. When the fermented material falls, it slides down to the bottom of the slope,
In addition, if the immature fermented product with poor water content control falls, the water content
A variable angle of 30-60 degrees to temporarily stay in including its own weight
And form an inclined surface with a length set to about 15 m ,
Also, an apparatus for promoting fermentation of organic sludge using an inclined surface, which forms a deposition site for sliding down and depositing a primary fermented material with good moisture adjustment at the lower end position of the inclined surface. 3. The primary fermented material that has reached the sedimentation site is set to a large volume that allows the outside air to pass through, is packed in a bag, and is stored for a predetermined period of time to allow the secondary fermentation to be performed. Method for promoting fermentation of organic sludge used.