JPWO2009116170A1 - Organic sludge recycling equipment - Google Patents

Abstract

An organic sludge recycling apparatus that efficiently dries organic sludge to a substantially uniform moisture content and compresses the volume of the dried sludge for easy handling. The present invention includes a sludge supply device, a drum dryer, and a pelletizing device. The sludge supply device is capable of rotating a substantially star-shaped rotary blade 21 between the crushing means 10 for collapsing the organic sludge in the supply hopper 1 by air pressure and each of a plurality of plate-like fixed blades 22. And a crushing quantitative supply means 20 arranged in the above. The drum dryer supplies organic sludge from the upper surfaces of two rotating heating drums 3 provided in parallel, adheres them to the surface of the heating drum 3 in a sheet form, and scrapes the dried sludge. Moreover, the pelletizing apparatus 50 pushes dry sludge into the type | mold 52, and shape | molds it into a pellet of 0.2-10 cubic centimeters. [Selection] Figure 1

Description

  The present invention relates to a technology for converting sewage sludge and organic sludge discharged from a food processing plant into effective resources such as fuel and fertilizer, and more particularly to an apparatus for producing dried pellets.

  For example, sewage sludge is partly reused as fertilizer, but most of it is dehydrated to dehydrated sludge and incinerated. Although incineration is harmless ash, it can be said that it is an excellent treatment method in that there are no problems later, but dehydrated sludge has a moisture content of 80-85%, requires fossil fuels such as heavy oil, and incineration costs increase. In addition, there is a problem that a large amount of carbon dioxide gas is generated.

Therefore, a system has been developed in which dehydrated sludge is dried to a moisture content that can be self-heated by a dryer and then incinerated. The boiler is operated using this incineration heat and the generated steam is supplied to the dryer. (For example, Patent Document 1). In this system, the incinerator is a stepped stoker furnace or a fluidized bed furnace, and the dryer is a disk type dryer that dries dehydrated sludge to a moisture content of 35-40%.
Also, a drum dryer that dries dehydrated sludge to a heating drum and dries the moisture content to 40 to 20%, and a pyrolysis furnace in which this dried sludge is equipped with a heat exchanger in the furnace and burns flamelessly in an oxygen-deficient state. In some cases, steam obtained by a heat exchanger is used as a heat source for a drum dryer (Patent Document 2).

JP 2004-278950 A Utility model registration No. 3188784

The sludge treatment system of Patent Literature does not require auxiliary fuel for incinerating sludge. In particular, the system of Patent Literature 2 is characterized in that no harmful substances are discharged and installation space is small and construction costs are low. .
However, it is not easy to dry the dewatered sludge with a drum dryer to obtain a moisture content within a predetermined range, and there is a problem that only dry sludge with unevenness can be obtained.
Further, the incineration heat is not sufficient for use only as a heat source for the heating drum, and there is a problem that it is difficult to effectively use it as energy. For example, it is possible to cover the power of the sludge treatment system by converting it to electric power, but the equipment cost is high and it cannot be said that it is practical.

The inventors have made various studies on the above-mentioned problems. Regarding the former point, the dewatered sludge from the treatment plant is not homogeneous and is in a state where various water contents are mixed. I found out that it is easy to be in the state.
In addition, although the feed apparatus which provided many blade | wings on the horizontal axis | shaft was provided in the lower part of the supply hopper, it is for guide | inducing sludge to an inlet and cannot lump-up sludge.
On the other hand, the latter is thought to be caused by simply drying the sludge, which is bulky even if it is used as fuel and is not easy to handle, and is difficult to use actively.

  Therefore, an object of the present invention is to provide an organic sludge recycling apparatus that efficiently dries organic sludge to a substantially uniform moisture content and that compresses the volume of the dried sludge to make it easy to handle. .

  In order to achieve the above object, the sludge supply device for a drum dryer of the present invention employs the following means. That is, according to the first aspect of the present invention, there is provided an organic sludge resource recovery device comprising a sludge supply device, a drum dryer, and a pelletizing device, wherein the sludge supply device supplies the organic sludge to the drum dryer. Crushing and quantification with an abbreviated star-shaped rotary blade arranged between each of a plurality of plate-like fixed blades at the lower part of the crushing means that collapses organic sludge nodules with air pressure in the lower part of the inside The drum dryer is configured to supply organic sludge from the upper surface of two rotating heating drums provided in parallel, adhere to the surface of the heating drum in a sheet form, and scrape the dried sludge. The pelletizing apparatus is characterized in that the dried sludge is pushed into a mold and formed into pellets of 0.2 to 10 cubic centimeters.

Organic sludge includes sewage sludge and waste sludge discharged from food processing plants.
In addition, in order to obtain the properties required for recycling, for example, when high thermal power fuel is required, necessary components such as adding pulverized coal or adding necessary components to make an appropriate fertilizer May be added as appropriate. The addition is preferably mixed with sludge dried with a drum dryer. The size of the pellet may be 0.2 to 10 cubic centimeters depending on the application to be used. For example, in the case of fuel, it is desirable to set the size to 0.5 to 3 cubic centimeters. The shape of the pellet is not particularly limited, such as a cylinder or a prism.

The sludge supply device, drum dryer, and pelletizing device can be most simplified if they are configured by directly connecting the inlet and outlet, but the overall equipment becomes higher and the construction cost of the building increases. The inlet for organic sludge will also be high.
In such a case, the supply hopper, the drum dryer, and the pelletizing device may be arranged side by side and connected by a conveyor.

  The drum dryer is a dewatered organic sludge with a moisture content of 75-85% that is attached to the heating drum in a sheet form and dried to a moisture content of 20-10%. Use the one provided in parallel. The heating source is not particularly limited, such as steam, heated oil, electric heater, etc., but an incinerator that uses pellets obtained by this resource recycling device as fuel is provided in the vicinity, and steam is generated in the boiler using this incineration heat. It is desirable to heat (Claim 3).

The agglomeration means is not particularly limited as long as it can crush the nodule-like sludge with air pressure, but it is easy to use a cylindrical one that is connected to an air source and has a large number of holes on the outer periphery. It is. The installation location is preferably the lower part of the supply hopper, but may be determined depending on the properties of the sludge, such as being provided in the middle of the supply hopper.
The crushing and quantitative supply means crushes sludge finely and sends out a fixed amount. A plurality of fixed blades are provided in parallel at regular intervals, and a number of substantially star-shaped rotary blades are rotatably provided between the fixed blades. It should be.

  According to a second aspect of the present invention, there is provided an organic sludge resource recovery device comprising a sludge supply device, a drum dryer, and a pelletizing device, wherein the sludge supply device supplies the organic sludge to the drum dryer. In the lower part of the inside, a clumping means for collapsing the organic sludge by air pressure, and in the lower part, a cylindrical body having a porous member fixed to the tip is rotatably mounted, and the organic extruded into the vicinity of the porous member The drum dryer is provided with a crushing and constant supply means provided with a rotary blade for converting sludge into a chip shape. It is attached to a sheet and scrapes off the dried sludge, and the pelletizing apparatus is characterized in that the dried sludge is pushed into a mold and formed into pellets of 0.2 to 10 cubic centimeters.

  This organic sludge recycling apparatus is the same as claim 1 except that the configuration of the crushing and quantitative supply means is different. The cylindrical body with the screw of the crushing and quantitative supply means pumps sludge and extrudes it linearly from the hole of the porous member fixed to the tip. The porous member may be a net.

  As described above, the organic sludge recycling apparatus of the present invention is provided with the sludge supply device comprising the agglomeration means for collapsing the organic sludge aggregate with air pressure and the crushing quantitative supply means. Is broken down, finely crushed by the crushing quantitative supply means, and sent to the heating drum in a fixed quantity. For this reason, sludge adheres to a heating drum in the form of a uniform sheet and can be dried almost uniformly.

In the crushing and quantitative supply means according to claim 1, a substantially star-shaped rotary blade is rotatably disposed between each of the plurality of plate-like fixed blades, so that the finely crushed sludge is reliably sent in a fixed amount. It is done.
The particle size can be adjusted by appropriately changing the interval between the fixed blades.
According to a second aspect of the present invention, there is provided a crushing and quantitative supply means comprising a rotary blade in which a screw is rotatably mounted in a cylindrical body having a porous member fixed to the tip thereof, and organic sludge pushed out in the vicinity of the porous member is chipped. Therefore, similarly to the above, the finely crushed sludge is reliably sent in a fixed amount. The size of the particles can be adjusted by changing the pore size of the porous member.

  Furthermore, since the dried sludge is pushed into a mold by a pelletizing device and formed into pellets of 0.2 to 10 cubic centimeters, the volume is compressed and it is easy to handle for use and transportation, such as solid fuel and fertilizer It can be used as an effective resource.

Embodiments of the organic sludge recycling apparatus according to the first aspect of the present invention will be specifically described below with reference to the drawings.
FIG. 1 is an explanatory view showing the entire organic sludge recycling apparatus, which is composed of a sludge supply device, a drum dryer 2 and a pelletizing device 50. The organic sludge is sewage sludge here.

As shown in FIG. 2, the sludge supply apparatus is configured by a supply hopper 1 into which sludge is charged, a crushing means 10 provided in the lower part thereof, and a crushing quantitative supply means 20 provided in the lower part thereof. Yes.
The feed hopper 1 is opened at the top, dehydrated, and sewage sludge having a water content of 80 to 85% is charged. In addition, the conveyor (not shown) is attached separately so that sludge may be supplied continuously according to the processing capacity of the drum dryer 2.

  The crushing means 10 includes a perforated cylinder 11 and a perforated cylinder 12 into which air pressure is introduced, and is fixed obliquely upward with respect to the lower side surface in the supply hopper 1. The tips of the perforated cylinders 11 and 12 are closed by blocking plates 11a and 12a. The perforated cylinder 11 is a pipe having a diameter of about 40 mm and a length of about 50 cm. The perforated cylinder 12 is a pipe having the same diameter and a length of 40 cm. It is said. A large number of holes 13 of about 10 mm are provided on each outer peripheral surface. Here, the air pressure is 7 kilograms per square centimeter.

The crushing and constant supply means 20 is provided between the discharge port of the supply hopper 1 and the input port 4 of the drum dryer 2, and is composed of a plurality of fixed blades 22 and a rotary blade 21 in a frame 20a. ing. The details of the fixed blade 22 and the rotary blade 21 are as follows. As shown in FIG. 3, a large number of plate-shaped fixed blades 22 are fixed to the connecting plate 24 at a predetermined interval (here, 12 mm). A large number of rotary blades 21 fixed to the shaft 23 are fitted into the shaft 23.
The rotary blades 21 have a substantially star shape with a thickness of about 10 mm and an outer diameter of about 130 mm. Each rotary blade 21 is fixed to the shaft 23 by shifting the blade little by little in the rotational direction. Yes. The shaft 23 is rotatably supported and is connected to a motor 24 provided on the frame body 20a via a chain. The fixed blade 22 is a plate having a thickness of about 10 mm, a height of about 80 mm, and a width of about 130 mm.

The drum dryer 2 has a slot 4 at the top of the frame 2a, takes in steam from the boiler, the surface is heated to 100 to 120 degrees Celsius, and the two heating drums 3 rotate. A scraping blade 5 is provided to scrape dry sludge that adheres to and dries.
FIG. 4 is a perspective view showing the entire sludge dryer 2 with the upper cover removed, and 6 is a motor for rotating the heating drums 3 and 3 inward (in the direction of the arrow in FIG. 1). To the heating drums 3 and 3. 7 is a bearing of a reduction shaft, and 8 is a steam pipe from the boiler. Further, 9 is a sludge overflow stopper and 26 is a dried sludge discharge port (see FIG. 1).

The pelletizing apparatus 50 is connected from the discharge port 26 of the drum dryer 2 by the transport conveyor 40, and a roller 54 and a mold 52 that rotate around a vertical shaft 56 are accommodated in a case 51.
The case 51 is divided into a supply chamber 51a, a discharge chamber 51b, and a power chamber 51c. The supply chamber 51a is provided with two rollers 54 connected by a connecting shaft 53. The roller 54 is rotatably attached to the connecting shaft 53 via a bearing.
The connecting shaft 53 is connected to a vertical shaft 56, and a large bevel gear 56 is fixed to the vertical shaft 56 in the power chamber 51 c and meshes with a small bevel gear 57 connected to a motor 58. Therefore, the roller 54 rolls by the rotation of the vertical shaft 56.

A mold 52 having a large number of mold holes 52a is fixed at the boundary between the supply chamber 51a and the discharge chamber 51b, and the roller 54 is provided so as to roll on the mold 52 (the mold hole 52a portion).
A large number of mold holes 52a are provided on the circumference around which the roller 54 rolls, and have a diameter of 10 mm and a depth of 20 mm.

Next, the operation of the organic sludge recycling apparatus configured as described above will be described.
The sludge supplied to the supply hopper 1 is in a state in which lumps of various sizes are mixed, and there are voids in the supply hopper 1 everywhere.
The massive sludge is broken by the crushing means 10. That is, the air pressure is intermittently supplied to the perforated cylinder 11 and the perforated cylinder 12 and the air is blown into the supply hopper 1 from the hole 13 to break up the lump of sludge and break up the gap. The sludge that has been crushed is sequentially sent to the crushing and quantitative supply means 20.

In the crushing quantitative supply means 20, the rotary blade 21 driven by the motor 25 is continuously rotated, and the sludge placed between the blades of the rotary blade 21 is sequentially sent downward. Since each rotary blade 21 is provided with the blades slightly shifted in the rotational direction, sludge is intermittently discharged from one rotary blade 21, but as a whole, a fixed amount of sludge is always present. Discharged.
And the small lump sludge which was not crushed by the crushing means 10 is also crushed finely when passing between the fixed blades 22. The fine sludge is supplied to the heating drums 3 and 3 of the drum dryer 2 in a certain amount.

As described above, the sludge falling on the heating drums 3 and 3 at about 100 to 120 degrees Celsius is fine and always a constant amount. It is stretched on the 3rd and 3rd surfaces and adheres in the form of a sheet. Then, after the half rotation or more, it is scraped off by the scraping blade 5. This sludge has been dried to a moisture content of 20 to 10%. Then, it is sent almost quantitatively from the discharge port 26 to the pelletizing device 50 by the transport conveyor 40.
The degree of drying can be appropriately set by adjusting the amount of sludge supplied to the heating drums 3 and 3 and the surface temperature and rotation speed of the heating drums 3 and 3.

  The dried sludge sent to the supply chamber 51a of the pelletizing apparatus 50 is first pushed into a large-diameter portion on the upper end side of the mold hole 52a, and then the dried sludge placed thereon is trampled by a roller 54. Then, it is fed into the lower narrow mold hole 52a, compacted and sent to the discharge chamber 51b in the form of pellets. The pellet is discharged from the discharge port 59. Note that a device for filling the bag is separately provided at the discharge port 59.

FIG. 7 shows another embodiment of the first aspect of the present invention. In addition, since the pelletizing apparatus 50 from the conveyance conveyor 40 after the dryer 2 is the same as FIG. 1, it is abbreviate | omitting.
The difference from FIG. 1 is that the supply hopper 1 with the crushing and quantitative supply means 20 attached to the lower part and the drum dryer 2 are separated and connected by a conveyor 40. Thereby, installation is easy also in the case of a low building.

Next, an embodiment of the organic sludge recycling apparatus of the invention of claim 2 will be described based on FIG. 5 and FIG.
FIG. 5 is an explanatory view showing an organic sludge recycling apparatus, and corresponds to FIG. 1 of the above embodiment.
The supply hopper 1, the crushing means 10, the drum dryer 2, and the pelletizing device 50 are the same as those in the above embodiment, and the crushing and quantitative supply means 30 is different from the above. In addition, in FIG. 5, the conveyance conveyor 40 and the pelletization apparatus 50 which are apparatuses after the drum dryer 2 are abbreviate | omitted.

The crushing fixed amount supply means 30 rotates in the vicinity of the feed blade 31 provided at the discharge port of the supply hopper 1, the cylinder 32 in which the screw 33 is inserted and the porous member 32a is fixed at the tip, and the porous member 32a. The rotary blade 35 is constituted. A rear end upper portion of the cylindrical body 32 is connected to a discharge port of the supply hopper 1, and a motor 34 for driving the screw 33 is connected to the rear side.
The rotary blade 35 is provided in a case 37 and has a substantially cross shape driven by a motor 36. As shown in FIG. 6, four cutters 35 b are fixed to the circular plate 35 a and are arranged close to the porous member 32 a of the cylindrical body 32.

  Thus, since it is comprised, the sludge in the supply hopper 1 is sent into the cylinder 32 one by one by the feed blade 31 in the state where the lump was made fine by the crushing means 10 and the space | gap was lost. Then, the sludge is pumped by the screw 33, becomes a denser state, and is sequentially pushed out from the porous member 32a in a string-like state. Then, it is cut by the rotary blade 35 into fine particles. Therefore, as in the above embodiment, the sludge is stretched on the surfaces of the heating drums 3 and 3 and adheres in a sheet form, so that high-quality dry sludge can be obtained.

It is a whole explanatory drawing which shows embodiment in the resource recovery apparatus of the organic sludge of invention of Claim 1. It is a front view which shows the whole sludge supply apparatus. FIG. 2 is a perspective view showing the inside of the crushing and quantitative supply means 20. FIG. 2 is a perspective view showing the drum dryer 2. FIG. 3 is an overall explanatory view showing an embodiment of the organic sludge recycling apparatus according to the second aspect of the present invention. It is a perspective view which shows the crushing fixed quantity supply means 30 same as the above. FIG. 2 is an overall explanatory view showing another arrangement in the organic sludge recycling apparatus according to the first aspect of the present invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Supply hopper 2 Drum dryer 2a Frame 2b Transfer means 3 Heating drum 4 Input port 5 Scraping blade 6 Motor 7 Bearing 8 Steam piping 9 Overflow prevention 10 Agglomeration means 11 Perforated cylinder 11a Closing plate 12 Perforated cylinder 12a Closed Plate 13 Hole 20 Crushing quantitative supply means 20a Frame 21 Rotating blade 22 Fixed blade 23 Shaft 24 Connecting plate 25 Motor 26 Discharge port 30 Crushing quantitative supply means 31 Feed blade 32 Cylindrical member 32a Porous member 33 Screw 34 Motor 35 Rotary blade 36 Motor 37 Case 40 Conveyor 50 Pelletizer 51 Case 51a Supply chamber 51b Discharge chamber 51c Power chamber 52 Mold 52a Mold hole 53 Connecting shaft 54 Roller 55 Vertical shaft 56 Large bevel gear 57 Small bevel gear 58 Motor 59 Discharge port 60 Conveyor

Claims (3)

  An organic sludge recycling device comprising a sludge supply device, a drum dryer, and a pelletizing device, wherein the sludge supply device has organic sludge agglomerates in a lower portion of a supply hopper that supplies the organic sludge to the drum dryer. A crushing means that collapses by air pressure, and a crushing quantitative supply means in which a substantially star-shaped rotary blade is rotatably disposed between each of a plurality of plate-like fixed blades at the bottom thereof, and the drum drying The machine supplies organic sludge from the upper surfaces of two rotating heating drums provided in parallel, adheres to the heating drum surface in the form of a sheet, and scrapes off the dried sludge. An apparatus for recycling organic sludge, characterized in that the dried sludge is pressed into a mold and formed into pellets of 0.2 to 10 cubic centimeters.   An organic sludge recycling device comprising a sludge supply device, a drum dryer, and a pelletizing device, wherein the sludge supply device has organic sludge agglomerates in a lower portion of a supply hopper that supplies the organic sludge to the drum dryer. A crushing means that collapses by air pressure, and a rotary blade in which a screw is rotatably mounted in a cylindrical body having a porous member fixed to the tip thereof in a lower portion thereof, and organic sludge extruded in the vicinity of the porous member is formed into a chip shape. The drum drier is provided with organic sludge supplied from the upper surfaces of two rotating heating drums provided in parallel, adhered to the surface of the heating drum in the form of a sheet, and dried sludge. An apparatus for recycling organic sludge, characterized in that the pelletizing apparatus pushes dry sludge into a mold and molds it into pellets of 0.2 to 10 cubic centimeters.   The heating drum of the drum dryer is heated by boiler steam by heat obtained in an incinerator using organic sludge pellets obtained by the organic sludge recycling apparatus as fuel. Item 3. The organic sludge recycling apparatus according to Item 2.

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