JP6524145B2 - Transfer method of methane fermentation suitable material - Google Patents

Description

  The present invention relates to a method for transferring methane fermentation suitable material.

  At present, in the energy use of bagged combustible waste (city waste), waste incineration power generation using the heat generated by incineration is mainly used to burn bagged combustible waste in an incinerator. BACKGROUND ART Biogas power generation is attracting attention, which generates biogas (methane) obtained by fermenting organic waste in waste as a fuel for an internal combustion engine, an external combustion engine or a fuel cell. The energy utilization of the bagged combustible waste in the biogas power generation is useful because the waste to be incinerated can be reduced and the number and burden of incinerators which are large equipment can be reduced.

  By the way, the methane fermentation apparatus which takes out methane from the bagged combustible waste decomposes the organic matter by microorganisms in the anaerobic environment (methane fermentation) to generate methane gas, and in particular, the inorganic matter not involved in the methane fermentation is a residue Naturally, the more methane fermentation unsuited substances that are not involved in this methane fermentation, the more residue there is, so it takes extra time and cost to process this residue, so how much it can be packed into combustible waste It is important to obtain suitable methane fermentation suitable for methane fermentation.

  Therefore, the present applicant selects a device for obtaining methane fermentation suitable substances from combustible waste (sorting of waste suitable for methane fermentation such as potatoes and paper, and waste suitable for incineration treatment such as vinyl and cloth) As an apparatus), the manufacturing apparatus of the methane fermentation suitable thing disclosed by Japanese Patent Application No. 2017-118908 is proposed.

  With this apparatus, a suitable substance for methane fermentation having a high concentration of organic matter and a small amount of residue after methane fermentation treatment can be easily and surely obtained.

Japanese Patent Application No. 2017-118908

  By the way, methane fermentation suitable ones are manufactured in the waste incineration plant where combustible wastes are collected, while this methane fermentation suitable ones are generally methane fermentation treated in another facility (for example sewage treatment plant), Heretofore, it has been desired to provide a method for transferring the methane fermentation suitable product from the production facility to the treatment facility.

  In view of the high fluidity of the methane fermentation suitable produced by the above-described apparatus for producing methane fermentation suitable according to the present invention, the present invention is very effective as a method for transferring the methane fermentation suitable produced at the production facility to a processing facility. Provides a practical method for transferring suitable methane fermentation products.

  The subject matter of the present invention will be described with reference to the accompanying drawings.

The methane fermentation preferred product E produced by the production facility 50 below 1 A method of transferring to the processing facility 51 to the methane fermentation, methane having fluidity from bagging combustible waste A below 2 at the manufacturing facility 50 The processing facility is manufactured from the manufacturing facility 50 by the transport vehicle 40 provided with the suction tank with a suction pump 40a for producing the fermentation suitable material E and containing the methane fermentation suitable material E or the transfer piping part 41 provided with the transportation pump 41a. 51. A transfer method of methane fermentation suitable material comprising transferring the methane fermentation suitable material E to 51.
1
A first sorting unit 2 for sorting the bag-broken waste B that has been subjected to bag-break processing by the dry sorting means, and the first sorting unit 2 A manufacturing facility 50 comprising: a second sorting unit 3 for adding the selected particle size difference sorting processed waste C by the water adding unit 1 and sorting the specific gravity difference by the wet sorting means.
Note 2
Methane fermentation suitable material E having a water content of 70% by weight or more and a diameter of 25 mm or less.

  Moreover, in the transfer method of the methane fermentation suitable thing of Claim 1, the said conveyance vehicle 40 is a vacuum car, It concerns on the transfer method of the methane fermentation suitable thing characterized by the above-mentioned.

  Moreover, in the transfer method of the methane fermentation suitable thing in any one of Claims 1 and 2, the said manufacturing facility 50 is a refuse incineration facility, It concerns on the transfer method of the methane fermentation suitable thing characterized by the above-mentioned. .

  Moreover, in the transfer method of the methane fermentation suitable thing in any one of Claims 1-3, the said treatment facility 51 is a sewage treatment facility, It concerns on the transfer method of the methane fermentation suitable thing characterized by the above-mentioned. .

  Since the present invention is as described above, the methane fermentation suitable product can be transferred from the production facility to the treatment facility by taking advantage of the high fluidity of the methane fermentation suitable product in which good fermentation is performed. And so on, which is a method for transferring a suitable substance for methane fermentation which exerts an unprecedented effect.

It is explanatory drawing of the transfer method of the methane fermentation suitable material which concerns on a present Example. It is explanatory drawing of the transfer method of the methane fermentation suitable material which concerns on a present Example. It is operation | movement explanatory drawing of the principal part which concerns on a present Example. It is operation | movement explanatory drawing of the principal part of a present Example. It is operation | movement explanatory drawing of the principal part of a present Example. It is explanatory drawing of the principal part of a present Example. It is explanatory drawing of the principal part of a present Example. It is operation | movement explanatory drawing of the principal part of a present Example. It is operation | movement explanatory drawing of the principal part of a present Example. It is a pie chart which shows the composition of the methane fermentation suitable material which concerns on a present Example. It is a pie chart which shows the composition of the methane fermentation suitable material which concerns on a present Example.

  The preferred embodiments of the present invention will be briefly described by showing the operation of the present invention based on the drawings.

  The present invention manufactures methane fermentation suitable material E having fluidity from combustible waste A at a manufacturing facility 50 for methane fermentation suitable material E, and carries the transport tank provided with a sealed tank 40a with a suction pump for storing the methane fermentation suitable material E It is fluidly transferred from the manufacturing facility 50 to the processing facility 51 by a transfer piping section 41 provided with a car 40 or a transfer pump 41a.

  Since the methane fermentation suitable product E manufactured at the manufacturing facility 50 has high fluidity, the transport vehicle 40 equipped with the suction tank with a sealed pump 40a or the transfer piping part 41 equipped with the transfer pump 41a efficiently and reliably It can be transferred from the manufacturing facility 50 to the processing facility 51, and the odor when transporting the methane fermentation product E can be reduced as much as possible.

  Specific embodiments of the present invention will be described based on the drawings.

  The present embodiment is a method of transferring the methane fermentation suitable product E manufactured in the manufacturing facility 50 for manufacturing the methane fermentation suitable product E to a processing facility 51 for performing methane fermentation.

  In the present embodiment, as illustrated in FIGS. 1 and 2, the manufacturing facility 50 is a waste incineration facility, and the treatment facility 51 is a sewage treatment facility, but all may be other facilities or dedicated facilities. It is good.

  In the manufacturing facility 50, the following manufacturing apparatus of the methane fermentation suitable material E is installed.

  Specifically, an apparatus for producing a methane fermentation suitable product E from the bagged combustible waste A, which is a torn bag portion 1 for breaking the bubbly combustible waste A, and the torn bag processed waste A first sorting unit 2 sorting B by dry sorting means, and a second sorting unit 3 sorting the waste C sorted by the first sorting unit 2 by differential sorting by wet sorting means It is equipped.

  In addition, the bagged combustible waste A is a combustible waste (city waste) which is packed in a plastic bag and discarded.

  Hereinafter, each component of the present embodiment will be described in detail.

  The bag-breaking portion 1 includes a pair of rotary shafts 14a and 14b having blade portions 14a 'and 14b' on the circumferential surface in a bag-breaking body 13 having a hopper 13a at the top as shown in FIGS. It is a structure (so-called double-axial bag-sealed structure) provided in an erected state at a horizontally opposed position via an interval.

  Further, the lower portion of the bag-breaking body 13 is provided in an open state, and is configured as a waste discharge portion 13b of the bag-treated waste B which is torn by the blade portions 14a 'and 14b'.

  Therefore, the bagged combustible waste A introduced from the hopper 13a is broken while passing between the rotating shafts 14a and 14b, and the broken bag-treated waste B is discharged from the waste discharge portion 13b. Exhausted.

  Further, in the present embodiment, a belt conveyor is provided below the dust discharge unit 13 b, and is configured as the first conveyance unit 15 that conveys the bag-free dust B to the first sorting unit 2.

  As shown in FIGS. 3 and 5, the first sorting unit 2 has a plurality of roller bodies 4 with a predetermined gap in the left and right wall portions 16a of the first sorting main body 16 including the left and right wall portions 16a and the bottom wall portion 16b. It has roller conveyance part 5 rotatably arranged in parallel via S, and each roller body 4 is comprised so that it may rotate in the same direction (conveyance direction).

  Protrusions 17 are juxtaposed on the circumferential surface of each roller body 4 at a predetermined interval T in the lengthwise direction of the roller body 4, and each of the protrusions 17 has a substantially triangular shape on the roller body 4. The plate material of is fitted and provided.

  Therefore, the one placed on the upper side by the rotation of the roller body 4 is conveyed by the friction with the projection 17.

  Further, in the roller conveyance portion 5, as shown in FIG. 6, a mesh-like sieve hole comprising a gap S between the adjacent roller bodies 4 and an interval T between the projection portions 17 provided on the respective roller bodies 4. A large number 2a is provided, and the eye width of the sieve hole 2a is set between 50 and 150 mm for both the gap S (longitudinal) and the interval T (horizontally long).

  Further, the bottom wall portion 16b of the first sorting main body 16 is provided in a tapered shape, the lowermost portion of the bottom wall portion 16b is provided in an open state, and it passes through the sieve hole 2a of the roller conveyance portion 5 It is comprised as refuse discharge part 16b 'of the refuse C1.

  Therefore, among the broken bags B transported by the roller transport unit 5, the passing falling debris C1 that has passed through the sieve holes 2a is discharged from the trash discharge unit 16b '.

  Further, the first sorting main body 16 is provided on the installation rack 18 as illustrated in FIG. 5, and one end portion (upstream side in the transport direction of the roller transport unit 5) of the length direction (transport direction) is installed The other end (downstream side of the roller conveyance unit 5 in the conveyance direction) is pivotally mounted on the gantry 18 so as to be vertically pivotable, and is connected to a lift 19 provided on the installation gantry 18.

  The elevating part 19 is constituted by a screw rod 19a erected so as to freely slide on the installation stand 18, and a movable cylinder 19b fitted in the screw rod 19a and moved up and down by screwing of a nut 19b ' The other end of the first sorting body 16 is pivotally connected to the cylinder 19b.

  Accordingly, the first sorting main body 16 can be tilted relative to the installation rack 18 by the operation of the lifting and lowering unit 19, and the roller transport unit 5 is tilted upward by a predetermined angle so that the downstream side in the transport direction is at the upper position. Become. In the present embodiment, the inclination angle of the roller conveyance unit 5 is set between 5 and 30 degrees.

  From the above, in the first sorting unit 2, when the garbage B subjected to the bag-breaking process is introduced to the roller conveyance unit 5, the passing falling dust C1 passing through and falling through the gap S (sieve hole 2a) between the rotating roller bodies 4; Inclined falling dust C2 which does not pass through and drop from the gap S between the bodies 4 (sieve holes 2a) and falls to the outside of the roller transport unit 5 from the sloped lower end of the roller transport unit 5, and the gap S between the roller bodies 4 It does not pass through the (sieve hole 2a) and is sorted into the over-inclination debris D which gets over the outside of the roller conveying portion 5 from the inclined upper end portion of the roller conveying portion 5. That is, the trash-treated waste B is sorted by the first sorting unit 2 by the dry sorting means.

  Further, in the present embodiment, a belt conveyor is provided below the dust discharge portion 16b ', and configured as the second conveyance portion 20 that conveys the dust C (passing dust C1 passing through particle size difference sorting processing) to the second sorting portion 3. It is done. Although FIG. 3 illustrates that only the falling dust C1 passing through the second conveyance unit 20 is conveyed to the second sorting unit 3 as the dust C subjected to the particle size difference sorting process, the passing falling dust C1 and the inclined fall are illustrated. It is also possible to transport both the dust C2 to the second sorting unit 3 as the dust C subjected to the particle size difference sorting process. This is because the inclined falling waste C2 may also contain a large amount of a substance to be the methane fermentation suitable substance E.

  The second sorting unit 3 includes a screen sorting unit 9 and a water adding unit 10 for hydrolyzing the particle C sorted waste C introduced into the screen sorting unit 9 in the sorting main body 21 provided with a hopper 21a at one upper end. The first discharge unit 11 is provided at the lower position of the screen sorting unit 9 and the second discharge unit 12 is provided at the upper position of the screen sorting unit 9.

  Specifically, as shown in FIGS. 7, 8 and 9, the screen sorting unit 9 performs a large number of sorting on the circumferential surface opposing position of the shaft-like rotating body 7 provided with a plurality of crushing convex portions 6 on the circumferential surface. An arc plate-shaped screen body 8 provided with a hole 8a is attached.

  The shaft-like rotating body 7 is rotated by the operation of the drive source 24, and its rotational speed is set to 100 to 600 rpm. Preferably, the rotational speed is 300 to 500 rpm.

  Further, each crushing convex portion 6 has a swing hammer structure in which a base end portion is pivotally attached to the shaft-like rotating body 7 and is radially projected by centrifugal force accompanying the rotation of the shaft-like rotating body 7 The screen body 8 is configured to shred dust at the tip end.

  Further, each crushing convex portion 6 is arranged in parallel in the longitudinal direction of the shaft-like rotating body 7 so that the crushing convex portions 6 adjacent to each other in the longitudinal direction of the shaft-like rotating body 7 are shifted by 90 degrees. It arrange | positions helically, and it is comprised so that the refuse introduced from the hopper 21a may be sent in the inside of the crushing main body 21 from one end side to the other end side.

  Further, at the other end of the shaft-like rotating body 7, a winding and crushing convex portion 6 ′ is juxtaposed in the length direction of the shaft-like rotating body 7.

  The winding and crushing convex portion 6 'is provided in a convexly curved shape in the rotational direction, and is not arranged helically but linearly in the longitudinal direction of the shaft-like rotating body 7, Not only is the debris sent to the other end side of the main body 21 broken up, but it is also wound up upward (the second discharge unit 12 described later).

  The screen body 8 is a cylindrical body configured by combining a plurality of arc-shaped plate members, and is provided so as to be fitted to the shaft-like rotating body 7.

  Further, a large number of sorting holes 8a provided in the screen body 8 are circular, and in the present embodiment, the diameter of the sorting holes 8a is set to 10 to 25 mm.

  Further, the distance between the surface of the screen body 8 and the tip of the crushing convex portion 6 when the shaft-like rotating body 7 rotates is set to 5 to 20 mm. Desirably, this space | interval is 10 mm-15 mm.

  The water addition unit 10 is configured by providing a nozzle to which a water transfer unit (water source and transfer hose) (not shown) is connected to the lower part of the hopper 21a as shown in FIG.

  The amount of water jetted from the water adding portion 10 is appropriately controlled, and the water adding amount is in the range of 0 to 100% based on the weight of the waste, and in the present embodiment, the water adding rate in the water adding portion 10 is It is set to 10 to 50% per garbage C weight. This water addition makes it easy to crush by including water in the dust C subjected to particle size difference sorting treatment, and also contributes to reducing the load applied to the shaft-like rotating body 7 (drive source 24).

  The first discharge unit 11 is configured by providing the lower portion of the crushing main body 21 in an open state as illustrated in FIGS. 7, 8 and 9, and the dust of the sorting hole passing trash E sorted and sorted by the screen sorting unit 9. It is configured as a discharge unit.

  Therefore, among the dust C subjected to particle size difference sorting processing input from the hopper 21a, it is crushed at the crushing convex portion 6 and is hydrolyzed by the water adding portion 10 to become a heavy object, and the sorting hole passing through the sorting hole 8a of the screen body 8 The refuse E is discharged from the first discharge unit 11.

  In this embodiment, the container 22 is movably provided at the lower part of the crushing main body 21 and configured to receive the sorting hole passing waste E discharged from the first discharging portion 11.

  As shown in FIGS. 7 and 9, the second discharge portion 12 has a cylindrical body 23 communicating with the upper portion of the screen sorting portion 9 horizontally provided on the upper other end side of the crushing main body 21. A transport shaft 23a having a transport blade 23a 'formed in a spiral shape is provided on the circumferential surface.

  Therefore, among the refuse C having been subjected to particle size difference sorting processing input from the hopper 21a, it does not become crushed at the crushing convex portion 6 and does not become a heavy product even when it is hydrolyzed by the water portion 10 and passes through the sorting hole 8a of the screen body 8 The sorting hole non-passing waste F is rolled up by the rolling up and crushing convex portion 6 ′, sent to the cylindrical body 23, transported by the transport shaft 23a, and discharged from the tip.

  From the above, in the second sorting unit 3, when the dust C subjected to the particle size difference sorting treatment is introduced into the screen sorting unit 9 while being hydrolyzed by the water adding unit 10, the crushing convex portion 6 and the winding and breaking up are crushed with the rotation of the shaft-like rotating body 7 The sorting hole passing waste E which is crushed by the convex portion 6 ′ and discharged from the first discharge portion 11 through the sorting holes 8a of the screen body 8, and the crushing convex portion 6 and the winding crushing convex portion 6 ′ are not crushed It can not pass through the sorting hole 8 a of the body 8 and is rolled up and sorted into the sorting hole non-passing waste F discharged from the second discharge part 12. That is, the waste C subjected to the particle size difference sorting process is sorted by the wet sorting means by the second sorting unit 3.

  The code | symbol 30 is a refuse collection car which collects in the bag and collects the combustible waste A.

  The process for producing methane fermentation suitable product E using the apparatus for producing methane fermentation suitable product E configured as described above will be described.

  First, the bagged combustible waste A collected by the waste collection vehicle 30 is broken by the tearing portion 1.

  Subsequently, the bag-processed waste B subjected to the bag-breaking process is subjected to particle size difference sorting by the first sorting unit 2 by the dry sorting means.

  Specifically, when the bag-treated dust B is introduced into the roller conveyance unit 5, the passing drop dust C1 passing through and falling through the gap S between the rotating roller bodies 4 and the gap S between the roller bodies 4 passing through and falling The dust does not pass through the gap S between the roller members 4 and does not fall from the inclined lower end portion of the roller conveyance portion 5 to the outside of the roller conveyance portion 5 and from the inclined upper end portion of the roller conveyance portion 5 It is sorted into the over-the-slope debris T which gets over the outside of the roller conveyance section 5.

  The passing and falling dust C1 is, for example, a box or paper (small dust).

  The inclined falling dust C2 is, for example, paper, vinyl, or the like (large-sized, heavy dust that can not go over the slope).

  Although non-combustibles such as cans roll down, they can be easily removed with a magnetic separator etc. as the property of the collected material (less hanging at the time of removal with a suspension type magnetic separator etc.) Since the amount of water-containing matter is reduced, the amount of heat is high and the use for fueling etc. can be considered.

  For example, the over-inclination refuse D is a vinyl, a cloth (clothing), etc.

  In addition, since high moisture content potatoes and paper are preferentially recovered as the passing falling trash C1 as in the inclined falling trash C2, the high moisture content of the recovered material is reduced, and the amount of heat is high, so as to be converted to fuel etc. Can be used.

  As described above, both the passing-falling waste C1 and the inclined falling waste C2 sorted by the first sorting unit 2 are sent to the second sorting part 3 as the dust C subjected to the particle size difference sorting process, and the over-tilting waste D is fermented As waste that is not suitable for The reason why inclined fall waste C2 was also adopted as waste C subjected to particle size difference sorting was to give priority to an increase in the amount of recovered potatoes, and if better methane fermentation suitable material is to be obtained, only passing fall waste C1 is used as a particle size Adopted as differentially sorted waste C.

  Subsequently, the second sorting unit 3 sorts the difference in specific gravity of the dust C (passing trash C1 and inclined falling trash C2) sorted by the first sorting unit 2 by the wet sorting means.

  Specifically, when the dust C subjected to the particle size difference sorting treatment is introduced into the screen sorting unit 9 while being hydrolyzed by the water addition unit 10, it is crushed at the crushing convex portion 6 with the rotation of the shaft-like rotating body 7 and the screening of the screen body 8 is performed. The sorting hole passing waste E which passes through the hole 8 a and is discharged from the first discharging portion 11 and is not crushed by the crushing convex portion 6 and can not pass through the selecting hole 8 a of the screen body 8 and is rolled up from the second discharging portion 12 It is sorted into the sorting hole non-passing waste F to be discharged.

  The sorting hole passing waste E is, for example, paper, paper or the like (heavy waste which is easily broken up and finely broken by containing water).

  Furthermore, when this sorting hole passing waste E was confirmed, the ratio of the organic matter in the solid content of the sorting hole passing waste E (organic matter ratio) is 75 to 85% by weight, that is, the solid content (TS) is 17.2% by weight The organic matter concentration (loss on ignition) was 14.6% by weight, and the organic matter ratio (VS / TS) calculated therefrom was 84.9% by weight. The water content was 85% by weight or less, and the maximum diameter was 15 to 25 mm.

  Therefore, since the organic matter ratio is high, it can be said that the methane fermentation suitable material E has a small amount of residue after the methane fermentation treatment and also has high fluidity.

  The sorting hole non-passing waste F is, for example, vinyl or the like (light-weight waste which does not contain water and is difficult to be crushed).

  As described above, the sorting hole passing waste E sorted by the second sorting unit 3 is used as a methane fermentation suitable substance E, and the sorting hole non-passing waste F is treated as waste not suitable for fermentation (incineration and the like).

  The graphs of FIGS. 10 and 11 show the composition of the methane fermentation suitable material E (the waste passing through the sorting hole) in the two fractionation tests performed using the above-described apparatus for producing a methane fermentation suitable material.

  From this test, the ratio of impurities (such as vinyl, metal, mineral such as stone, etc.) in the methane fermentation suitable material E is as low as 1 to 8%, so the diameter of the methane fermentation suitable material E is small and hard to clog, It is difficult to cause blockages in the piping, in the pump, and in the sewerage facility at the time of pump pumping, and it is possible to prevent the failure of the pump such as the pump, and to ensure the maintenance and manageability of the facility and maintainability.

  Next, as illustrated in FIGS. 1 and 2, the treatment facility 51 is an existing treatment facility (sewage treatment facility) provided with a methane fermentation tank 51 a and a generator.

  Further, in the present embodiment, a means for transferring the methane fermentation suitable product E manufactured at the manufacturing facility 50 to the processing facility 51 is provided.

  Specifically, FIG. 1 shows a transport vehicle 40 (vacuum car) equipped with a suction tank with a suction pump 40a moving between the manufacturing facility 50 and the processing facility 51 as means for transferring the methane fermentation suitable substance E. FIG. 2 shows the case where the transfer piping unit 41 provided with the transfer pump 41a between the manufacturing facility 50 and the processing facility 51 is adopted, and in any case methane fermentation from the manufacturing facility 50 to the processing facility 51 The preferred product E is configured to be fluidly transferred.

  The code | symbol 40b is a hose extended from a suction pump.

  A transfer method using the transfer means according to the present embodiment having the above configuration will be described.

  The methane fermentation suitable material E having fluidity was manufactured from combustible waste at the manufacturing facility 50, and the methane fermentation suitable material E was provided with a closed tank with a suction pump for moving between the manufacturing facility 50 and the treatment facility 51. The transfer piping unit 41 provided with a transfer pump provided between the transfer vehicle 40 or the manufacturing facility 50 and the processing facility 51 fluidly transfers the manufacturing facility 50 to the processing facility 51 (see FIGS. 1 and 2).

  Therefore, according to the present embodiment, since the methane fermentation suitable product E manufactured in the manufacturing facility 50 has high fluidity, the transfer piping provided with the transport vehicle 40 provided with the suction tank with a suction pump 40a or the delivery pump 41a. By the part 41, it can transfer to the processing facility 51 from the manufacturing facility 50 efficiently and reliably, and moreover, the odor at the time of conveying the methane fermentation suitable thing E can be reduced as much as possible.

  Further, in the present embodiment, since the transport vehicle 40 is a vacuum car, the above-described effects can be reliably achieved.

  Further, in the present embodiment, since the manufacturing facility 50 is a waste incineration facility, the existing facility can be effectively used. That is, the residue (fermentation unsuitable material) which must be incinerated generated in the manufacturing process of the methane fermentation suitable material E can be processed with the incinerator which exists in a plant | facility.

  Further, in the present embodiment, since the treatment facility 51 is a sewage treatment facility, the existing facility can be effectively used. That is, conventionally, there is no method for transferring a sufficient amount of the methane fermentation suitable substance E, and the methane fermentation tank provided in the sewage treatment facility has a vacant capacity, but the methane fermentation preferable substance E is Being able to transfer well, processing can be performed using the above-mentioned free capacity of the methane fermenter.

  In addition, in this embodiment, when constructing the processing facility 51, the construction is difficult unless the facility scale is a certain degree, but in this respect, the volume is obtained by transferring the methane fermentation suitable material E from the manufacturing facility 50 in various places. And construction of facilities is possible (scale benefits can be obtained).

  The present invention is not limited to this embodiment, and the specific configuration of each component can be designed as appropriate.

A bag stuffed combustible waste
B bag-treated waste
C Particle size difference sorting processed waste E Methane fermentation suitable
1 Broken bag part
2 first sorting section
3 second sorting unit
40 Carrier
40a Sealed tank
41 Transfer piping section
41a Transfer pump
50 manufacturing facilities
51 processing facility

Claims (4)

The methane fermentation preferred product E produced by the production facilities below 1 A method of transferring to the processing facility for methane fermentation, the methane fermentation preferably having a fluidity below 2 from bagging combustible waste in the manufacturing facility Transporting the methane fermentation suitable product from the manufacturing facility to the processing facility by a transport vehicle equipped with a transport vehicle or a transport pump having a sealed tank with a suction pump for producing and storing the methane fermentation preferred material The transfer method of the methane fermentation suitable thing characterized by the above.
1
Bag-filling section for bag-filling combustible waste, first sorting section for sorting the broken bags subjected to bag-breaking waste by differential sorting using dry sorting means, and particle size difference sorted by the first sorting section A manufacturing facility provided with a second sorting unit that hydrolyzes sorted waste by a water addition unit and performs specific gravity difference sorting by wet sorting means.
Note 2
Methane fermented material having a moisture content of 70% by weight or more and a diameter of 25 mm or less.   The method for transferring methane fermentation suitable material according to claim 1, wherein the transport vehicle is a vacuum car.   The method for transferring a suitable substance for methane fermentation according to any one of claims 1 and 2, wherein the production facility is a waste incineration facility.   The method for transferring methane fermentation suitable material according to any one of claims 1 to 3, wherein the treatment facility is a sewage treatment facility.

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