JP5872521B2 - Methane fermentation tank and method for removing deposits in methane fermentation tank - Google Patents

Description

  The present invention relates to a methane fermentation tank for anaerobic fermentation treatment of organic waste such as sewage sludge and food waste, and a method for removing deposits in the methane fermentation tank.

  As a technique for discharging the contents in the methane fermentation tank to the outside of the tank, there is a technique described in Patent Document 1, for example. The technique described in Patent Document 1 is a technique for extracting sludge from the methane fermentation tank main body (digestion tank main body). A discharge pipe (overflow pipe) is installed vertically along the inner wall of the digestion tank body, and one end of the discharge pipe (sludge inlet) is positioned at the bottom of the digestion tank body, and at the top of the discharge pipe (overflow pipe) An air release means (a cylinder having an upper end positioned above the liquid level upper limit level in the digestion tank body) is provided.

  According to this configuration, Patent Document 1 states that sludge can be discharged stably without providing a concrete sludge pocket in the digestion tank body.

JP 2004-105798 A

  As the digestion tank continues to operate, sand, which has a higher specific gravity than sludge, accumulates at the bottom of the digestion tank body. Also, highly viscous sludge may stick to the bottom of the digester tank body and accumulate.

  Here, the technique described in Patent Document 1 relates to a method of extracting sludge from the digestion tank main body in order to send it to a sludge dewatering facility, such as sludge containing a large amount of sand deposited on the bottom of the digestion tank main body. It does not relate to a method for discharging sediments out of the tank.

  Furthermore, in the sludge discharging method (pullout method) described in Patent Document 1, it is almost impossible to discharge the deposits out of the tank. The extraction of the sludge described in Patent Document 1 is due to the natural flow of the fermented liquid (sludge) using only the difference in liquid level (the liquid flows from a high place to a low place), and thus contains a large amount of sand. It is difficult to discharge accumulated sludge and highly viscous sludge stuck to the bottom of the digestion tank body.

  Therefore, conventionally, after the digestion tank has been operated for a certain period of time, the gas layer in the digestion tank body is purged with nitrogen, and then the digestion tank body is opened and cleaned to remove deposits in the digestion tank body. Has been made. Although the size of the digestion tank varies, this cleaning operation is very large and difficult.

  In addition, unless the cleaning operation in the digestion tank body is performed, deposits are accumulated in the digestion tank body. As the deposit in the digestion tank increases, the effective capacity of the digestion tank decreases accordingly, and as a result, the amount of methane gas generated from the digestion tank decreases.

  For this reason, there is a demand for a method capable of easily discharging deposits in the digestion tank body to the outside of the tank without opening the digestion tank body.

  The present invention has been made in view of the above circumstances, and its purpose is to easily discharge deposits in the methane fermentation tank main body to the outside of the tank without opening the methane fermentation tank main body, and It is providing the methane fermenter provided with the structure which can implement the method.

  The present invention is a method for removing deposits in a methane fermenter. By depositing liquid into the bottom of the methane fermentation tank main body, the deposit deposited on the bottom is migrated, and the migrated deposit is discharged out of the tank by the discharge means.

  The present invention is also an invention of a methane fermenter. The methane fermenter of the present invention includes a methane fermenter main body, liquid injection means for injecting liquid into the bottom of the methane fermenter main body, and deposits deposited at the bottom of the methane fermenter main body to the outside of the tank. And a discharging means that causes the deposit to migrate with the liquid press-fitted from the liquid press-fitting means, and the migrated deposit is discharged out of the tank by the discharging means.

  According to the present invention, deposits in the methane fermentation tank main body can be easily discharged out of the tank without opening the methane fermentation tank main body.

It is a side view which shows the methane fermenter which concerns on 1st Embodiment of this invention. It is AA sectional drawing (FIG. 2 (a)) of FIG. 1, and BB sectional drawing (FIG.2 (b)). It is a side view which shows the methane fermenter which concerns on 2nd Embodiment of this invention. It is a side view which shows the methane fermenter which concerns on 3rd Embodiment of this invention. It is AA sectional drawing of FIG.

  Hereinafter, embodiments for carrying out the present invention will be described with reference to the drawings. In the following description, as an example of the methane fermentation tank according to the present invention, a so-called digestion tank for anaerobic fermentation treatment of sewage sludge is illustrated, but the present invention is organic such as food waste. It can also be applied to a methane fermentation tank for anaerobic fermentation of waste.

(First embodiment)
(Configuration of digestion tank)
As shown in FIG. 1, a digestion tank 100 (methane fermentation tank) includes a digestion tank body 1 (methane fermentation tank body), a stirrer 2, a heating device 5, a liquid press-fitting device 3 (liquid press-fitting means), and a discharge device 4 ( Discharge means).

(Digestion tank body)
The digestion tank body 1 is a tank for anaerobic fermentation treatment of sludge (sewage sludge). The sludge charged into the digestion tank body 1 is heated by the heating device 5 and stirred by the stirrer 2. Digestion gas generated by anaerobic fermentation comes out from the top of the tank. In addition, illustration of the sludge input means to the digestion tank main body 1 and the digestion gas extraction means from the digestion tank main body 1 is omitted. The digestion gas is a gas (biogas) of about 60% by volume of methane and about 40% by volume of carbon dioxide.

  Here, the digestion tank body 1 of the present embodiment is made of a steel plate. On the other hand, the digestion tank body described in Patent Document 1 is made of concrete (made of prestressed concrete). The concrete digestion tank body has a long production period and high production costs. If the digestion tank body 1 made of steel plate is used as in the present embodiment, the production period can be shortened and the production cost can be reduced as compared with the digestion tank body made of concrete.

  In addition, prestressed concrete cannot be perforated after being formed. For this reason, it is not difficult to provide branch press-fit pipes 22a to 22g, which will be described later, constituting the liquid press-fitting apparatus 3 so as to penetrate the digestion tank body, but it is very difficult (manufacturing time and cost are high). On the other hand, steel plates are excellent in workability. Therefore, if the digestion tank body 1 is made of a steel plate as in this embodiment, it is easy to provide the branch press-fit pipes 22a to 22g that penetrate the digestion tank body. Moreover, it is easy to provide the digestion tank body 1 with an inspection port or attach various measuring devices. From these, by making it the digestion tank main body 1 made from a steel plate, while being able to shorten the production period, production cost can be held down. Furthermore, improvement in maintenance can be expected.

  In the present embodiment, the digestive tank body 1 has a vertical cylindrical shape. The bottom of the digestion tank body 1 is flat and installed horizontally. The bottom of the digestion tank body 1 may have an inverted conical shape whose center is slightly lower than the outer periphery. In this case, the inclination angle of the conical surface with respect to the horizontal direction is set to 5 degrees or less. Furthermore, the bottom of the digestion tank body 1 may have a conical shape whose center is slightly higher than the outer periphery. In this case, the inclination angle of the conical surface with respect to the horizontal direction is set to 5 degrees or less as in the case of the inverted conical shape. That is, the bottom of the digestion tank body 1 may be an angle of ± 5 degrees or less with respect to the horizontal direction toward the center, and further an angle of ± 3 degrees or less.

  The shape of the digestion tank body 1 may be a rectangular parallelepiped. Also in this case, the bottom of the digestion tank body 1 may be flat (flat and horizontally installed), its center may be slightly lower than the outer periphery (inverted quadrangular pyramid shape), or slightly higher. (Square pyramid shape). That is, the bottom of the digestion tank body 1 may be an angle of ± 5 degrees or less with respect to the horizontal direction toward the center, and further an angle of ± 3 degrees or less.

(Agitator)
The stirrer 2 disposed inside the digestion tank body 1 is for stirring the sludge (organic waste) introduced into the digestion tank body 1. In this embodiment, although it is set as the stirrer which stirs sludge with the blade | wing 2a rotated in the horizontal direction made from a steel plate, a draft tube type stirrer as described in patent document 1 may be used and generally used. A gas agitation type in which agitation is performed using the gas generated in the tank is also possible. The agitator 2 is disposed at the center of the digestion tank body 1 in plan view.

(Heating device)
The heating device 5 is for heating the sludge charged into the digestion tank body 1. The heating device 5 includes a circulation pump 15, a heater 16 (heat exchanger), and a sludge circulation pipe 17. Warm water is supplied to the heater 16 from a hot water source such as a boiler (not shown). The sludge extracted from the digestion tank body 1 is heated by the heater 16 and then returned to the digestion tank body 1.

(Liquid press-fitting device)
The liquid press-fitting device 3 is for causing a deposit S deposited on the bottom of the digestion tank body 1 to migrate with the press-fitted liquid by press-fitting liquid into the bottom of the digestion tank body 1. The deposit S is a sludge containing a lot of sand or a high-viscosity sludge.

The liquid press-fitting device 3 includes a liquid supply pump 11 and a press-fit liquid pipe 12 connected to the liquid supply pump 11. The liquid that is press-fitted into the digestion tank main body 1 may be anything as long as it is liquid, for example, sewage treated water.
Instead of using the liquid supply pump 11, the liquid may be pressed into the digestion tank body 1 under natural flow. For example, a water tank (not shown) may be installed at a position sufficiently higher than the liquid level in the digestion tank main body 1, and the liquid may be press-fitted under natural flow from the water tank to the digestion tank main body 1.

  The press-fit liquid pipe 12 in the present embodiment includes a discharge header pipe 21 connected to the liquid supply pump 11 and a plurality of branch press-fit pipes 22 a to 22 g connected to the discharge header pipe 21.

As shown in FIGS. 1 and 2B, the downstream side of the discharge header pipe 21 has a slightly larger diameter than the outer diameter of the digestion tank body 1 so as to surround the bottom side wall portion of the digestion tank body 1. It is a ring-shaped tube. The branch press-fit pipes 22a to 22g are connected to the ring-shaped pipe portion.
It is possible to install the discharge header pipe 21 in the digestion tank body 1 by reducing the discharge header pipe 21 (with a reduced diameter).

  The branch press-fit pipes 22 a to 22 g are provided so as to penetrate the bottom of the digestion tank body 1. Of the branch press-fit pipes 22a to 22g, the branch press-fit pipes 22a to 22f are provided at equal intervals along the outer periphery of the bottom of the digestion tank body 1. On the other hand, one of the branch press-fit pipes 22 a to 22 g is provided so as to extend toward the bottom center of the digestion tank body 1.

  Here, the discharge ports 23a to 23f of the branch press-fit pipes 22a to 22f arranged at the bottom end portions in the digestion tank main body 1 indicate that the discharge direction of the liquid from the respective discharge ports 23a to 23f is the same as the digestion tank main body 1. It is set as the direction which goes diagonally upward with respect to the bottom face (horizontal direction) of this, and goes to the center part (in this embodiment, the part where the upper blade | wing 2a of the stirrer 2 is arrange | positioned) of the digestion tank main body 1. FIG.

  In addition, as for the discharge direction (discharge angle) of the liquid from the discharge ports 23a to 23f, a specific discharge direction (discharge angle) is determined by the expected accumulation shape of the deposit S. Is preferably in the range of 15 ° to 80 °, that is, 15 ° to 80 ° (determined within the range of 15 ° to 80 °).

  Further, the discharge port 23g of the branch press-fit pipe 22g provided at the bottom center in the digestion tank main body 1 is such that the liquid discharge direction from the discharge port 23g is directed to the top plate portion 1a of the digestion tank main body 1. ing.

  Similar to the discharge direction (discharge angle) of the liquid from the discharge ports 23a to 23f, the discharge direction (discharge angle) of the liquid from the discharge port 23g depends on the expected deposit shape of the deposit S. (Discharge angle) is determined, but it is 30 ° to 90 ° with respect to the bottom surface of the digestion tank body 1, that is, a range of 30 ° to 90 ° (determined within a range of 30 ° to 90 °). Preferably).

  In the present embodiment, a total of six branch press-fit pipes 22a to 22f are arranged at the bottom end (outer periphery) of the digestion tank main body 1, and branch press-fit extending toward the bottom center of the digestion tank main body 1 is provided. Although one pipe 22g is disposed, a plurality of branch press-fitting pipes may be disposed only at the bottom end (outer periphery) of the digestion tank body 1 or toward the bottom center of the digestion tank body 1. Only the branch press-fit pipe 22g extending may be disposed. The branch press-fit pipes 22a to 22f may not be equally spaced along the outer periphery of the bottom of the digestion tank body 1. Furthermore, the branch press injection pipe arrange | positioned at the edge part (end part outer periphery) of the bottom part of the digestion tank main body 1 may be one.

  When only the branch press-fit pipe 22g (only one press-fit pipe) extending toward the bottom center of the digestion tank main body 1 is disposed, it is not appropriate to call this pipe “branch press-fit pipe”. Appropriately referred to as (pressed liquid pipe). In this case, the discharge header pipe 21 is unnecessary, and one end of the press-fit pipe (press-fit liquid pipe) is connected to the liquid supply pump 11. The position of the other end which is the discharge port of the press-fit pipe (press-fit liquid pipe) and the discharge direction therefrom are the same as those of the discharge port 23g of the branch press-fit pipe 22g.

(Discharge device)
The discharge device 4 is for discharging the deposit S migrated with the liquid press-fitted from the liquid press-fitting device 3 to the outside of the digestion tank body 1. The discharge device 4 includes a discharge pump 13 and a discharge pipe 14 connected to the discharge pump 13.

  The discharge pipe 14 in the present embodiment includes a suction header pipe 24 connected to the discharge pump 13 and a plurality of branch suction pipes 25 a to 25 g connected to the suction header pipe 24.

  As shown in FIGS. 1 and 2A, the upstream side of the suction header pipe 24 is a ring having a slightly smaller diameter than the inner diameter of the digestion tank body 1 along the inner wall portion of the bottom of the digestion tank body 1. The tube is shaped. And the branch suction pipes 25a-25g are connected to this ring-shaped pipe part.

  Of the branch suction pipes 25a to 25g, the branch suction pipes 25a to 25f are provided at equal intervals along the inner periphery of the bottom of the digestion tank body 1, and the respective suction ports 26a to 26f are opened downward. Yes. That is, the suction ports 26a to 26f of the branch suction pipes 25a to 25f are arranged at equal intervals along the side wall portion of the bottom portion in the digestion tank body 1 in a mode of opening downward.

  On the other hand, of the branch suction pipes 25a to 25g, one branch suction pipe 25g is connected to the suction header pipe 24 so as to extend toward the bottom center of the digestion tank body 1, and the suction port 26g The tank body 1 opens downward at the center of the bottom.

  In the present embodiment, a total of six branch suction pipes 25a to 25f are arranged along the inner periphery of the bottom of the digestion tank body 1, and a branch suction pipe 25g extending toward the bottom center of the digestion tank body 1; Although one is arranged, a plurality of branch suction pipes may be arranged only in a portion along the inner periphery of the bottom of the digestion tank main body 1, or a branch suction pipe extending toward the center of the bottom of the digestion tank main body 1 You may arrange only. The branch suction pipes 25 a to 25 f may not be equally spaced along the inner periphery of the bottom of the digestion tank body 1. Furthermore, the branch suction pipe arrange | positioned along the inner periphery of the bottom part of the digestion tank main body 1 may be one.

(Removal of sediment accumulated at the bottom of the digestion tank body)
Next, a method for removing the deposit S accumulated at the bottom of the digestion tank body 1 will be described.

  First, the liquid supply pump 11 is operated, and the liquid is pressed into the bottom of the digestion tank body 1 from the branch press-fit pipes 22a to 22g. The deposit S accumulated at the bottom of the digestion tank main body 1 migrates to the liquid phase portion in the digestion tank main body 1 by spraying the liquid from the liquid supply pump 11.

  Thereafter, the discharge pump 13 is operated to suck the migrated deposit S together with the fermented liquid (sludge) in the digestion tank body 1 from the branch suction pipes 25a to 25g and discharge it outside the tank.

  The activation of the liquid supply pump 11 (start of liquid injection) and the activation of the discharge pump 13 (start of extraction of the deposit S) may be performed at the same time or are discharged earlier than the activation of the liquid supply pump 11. The pump 13 may be activated. That is, the start of liquid press-in and the start of pull-out of the deposit S may be performed simultaneously, or the pull-out of the deposit S may be started earlier than the start of press-in of the liquid (the same applies to other embodiments). .

  The discharge ports 23a to 23g of the branch press-fit pipes 22a to 22g (press-fit liquid pipe 12) may have the same dimensions as the diameters of the branch press-fit pipes 22a to 22g (press-fit liquid pipe 12). By making the diameter (opening diameter) of 23 g smaller than the diameters of the branch press-fit pipes 22a to 22g, the injection speed of the press-fit liquid can be increased, and the deposit S can be further migrated (others) The same applies to the embodiment).

  In addition, regarding the discharge pipe 14, it is also preferable that the suction ports 26a to 26g of the branch suction pipes 25a to 25g are expanded in diameter toward the suction side (a trumpet shape). According to this configuration, the collection effect of the migrated deposit S can be enhanced (the same applies to other embodiments).

(Action / Effect)
In the present invention, by depositing liquid into the bottom of the methane fermentation tank main body, the deposit deposited on the bottom is migrated, and the migrated deposit is discharged out of the tank by the discharge means.
According to this configuration, by depositing sediment in the methane fermentation tank body, for example, sediment at the bottom of the methane fermentation tank body, which is a sludge containing a lot of sand or a high-viscosity sludge, can be easily discharged. It can be discharged out of the tank.
Moreover, in this structure, it is not necessary to open the inside of a methane fermentation tank main body. That is, the deposit in the methane fermentation tank main body can be easily discharged out of the tank without opening the inside of the methane fermentation tank main body.

Further, in the present invention, as exemplified as the equipment configuration in the above-described embodiment, the methane fermentation tank is obliquely above the bottom of the methane fermentation tank main body from the end of the bottom in the methane fermentation tank main body. It is preferable to press-fit the liquid toward the center of the main body.
Moreover, it is also preferable to press-fit a liquid from the center of the bottom in the methane fermentation tank body toward the top plate of the methane fermentation tank body.
The corners of the bottom in the methane fermentation tank main body and the bottom center in the methane fermentation tank main body are portions where deposits are likely to accumulate. By ejecting the liquid from these portions obliquely upward or toward the center of the tank body, the deposits in the methane fermentation tank body can be more reliably migrated.

In addition, regarding the discharge of the migrated deposit, as illustrated as the equipment configuration in the above-described embodiment, the deposit migrated from a plurality of locations along the bottom side wall in the methane fermentation tank main body is discharged out of the tank. It is preferable.
The part along the side wall at the bottom of the methane fermenter main body is once moved upward (pushed up) by the press-fitting liquid, and then the moving speed of the sediment that migrates and settles by its own weight is relatively slow. It is. By discharging the deposit from this portion to the outside of the tank, the effect of collecting and discharging the deposit can be enhanced.

  Moreover, it is also preferable to discharge | emit the deposit which migrated from the bottom center in a methane fermentation tank main body out of a tank by a discharge means. The center of the bottom of the methane fermentation tank main body is a part where the accumulation part tends to accumulate as described above. By discharging the deposit from this part to the outside of the tank, the deposit discharging effect can be enhanced. .

  In this embodiment, the digestion tank body 1 is made of a steel plate. As described above, the steel sheet is excellent in workability. Therefore, it is easy to provide the liquid press-fitting device 3 and the discharge device 4 as exemplified in the above embodiment in the methane fermentation tank main body. Moreover, it becomes easy to provide an inspection port in the methane fermentation tank main body and attach various measuring devices.

  In addition, in the conventional digestion tank main body (methane fermentation tank main body) made from prestressed concrete, if the liquid press-fitting device 3 and the discharge device 4 in this embodiment are provided in the lower part of the digestion tank main body (methane fermentation tank main body), it will be manufactured. Expensive. In addition, by making the methane fermentation tank main body made of a steel plate, it can be expected to improve the maintainability as compared with a conventional concrete one.

(Second Embodiment)
The second embodiment will be described with reference to FIG. In addition, the same code | symbol is attached | subjected about the same apparatus and piping which comprises the digestion tank 100 of 1st Embodiment.

  In the digestion tank 101 of the present embodiment, the sludge circulation pipe 17 and the discharge header pipe 21 of the press-fit liquid pipe 12 are connected to each other by a pipe 18.

  Here, the pipe 18 flows a part or all of the heated fermentation liquor (heated sludge) used for heating the sludge in the digestion tank main body 1 to the press-fitted liquid pipe 12 for a predetermined time to digest it. This is a heated sludge injection pipe for use as a press-fitting liquid into the bottom of the tank body 1 (hereinafter referred to as a heated sludge injection pipe 18).

  It is preferable to use unsterilized water having a pH of about 6 to 8 (for example, unsterilized sewage treated water) as the liquid to be pressed into the digestion tank body 1, but it is used for heating sludge in the digestion tank body 1. It is also preferable to use the heated fermentation liquor (heated sludge) as a liquid to be pressed into the digestion tank body 1. The temperature of the heated fermentation liquor (heated sludge) is higher than that of the deposit S collected at the bottom of the digestion tank body 1, and the heated fermentation liquor (heated sludge) is sprayed onto the deposit S by press-fitting. The migration of the deposit S can be further promoted. This is because, according to the heated fermentation broth (heated sludge), for example, it is easy to release physical adsorption between sands and physical adsorption between sand and sludge.

  In addition, you may make it take out fermentation liquid (sludge) from the part between the circulation pump 15 of the sludge circulation piping 17 and the warmer 16, and supply it to the bottom part in the digestion tank main body 1 as a press injection liquid. That is, you may make it use the fermented liquor (sludge) before heating with the warmer 16 as a press injection liquid.

In the present embodiment, the heated sludge press-fitting pipe 18 is not directly connected to the bottom of the digestion tank body 1 but connected to the discharge header pipe 21 of the press-fitted liquid pipe 12 downstream of the liquid supply pump 11. By doing so, the sewage treated water and the heated fermentation liquid (heated sludge) can be used together as a press-fit liquid.
Thereby, using only the discharge position (discharge ports 23a-23g) of the press-fit liquid, depending on the property of the deposit S, using only the sewage treated water, using only the heated fermentation liquid (heated sludge), It is possible to selectively use the press-fit liquid, such as using sewage treated water and warmed fermentation liquid (heated sludge) in combination. That is, many options for promoting migration of the deposit S can be provided.

  In addition, when non-sterilized water (for example, non-sterilized sewage treated water) having a pH of about 6 to 8 is used as the press-fit liquid without using the fermented liquid (sludge) as the press-fit liquid, the press-fit liquid is continuously supplied for a long time. If this is done, the fermentation liquor in the digestion tank main body 1 is diluted and cooled, which may reduce the amount of digestion gas generated. Therefore, the supply amount of the press-fitting liquid (for example, unsterilized sewage treated water) to the digestion tank body 1 is preferably set to 0.5% or less of the effective capacity of the digestion tank body 1.

  Moreover, when the operation for supplying the press-fitting liquid into the digestion tank main body 1 and the operation for discharging the deposition part S from the digestion tank main body 1 exemplified in the first embodiment and the second embodiment are automatic operation by a timer. The deposit S in the digestion tank main body 1 can be automatically discharged out of the tank periodically, and as a result, a reduction in the effective capacity of the digestion tank main body 1 can be easily prevented.

(Third embodiment)
The third embodiment will be described with reference to FIGS. In addition, the same code | symbol is attached | subjected about the same apparatus and piping which comprises the digestion tank 100 of 1st Embodiment.

(Liquid press-fitting device)
The liquid press-fitting device 6 according to the present embodiment includes a liquid supply pump 11 and a press-fit liquid pipe 19 connected to the liquid supply pump 11. The press-fit liquid pipe 19 includes a discharge header pipe 31 connected to the liquid supply pump 11 and a plurality of branch press-fit pipes 32 a to 32 h connected to the discharge header pipe 31.

The downstream side of the discharge header pipe 31 is a ring-shaped pipe along the inner wall surface of the bottom of the digestion tank body 1 and is disposed at the bottom of the digestion tank body 1. The branch press-fit pipes 32a to 32h are connected to the ring-shaped pipe portion.
The diameter of the discharge header pipe 31 may be larger than that of the present embodiment, and the discharge header pipe 31 may be disposed outside the digestion tank body 1.

  The branch press-fit pipes 32 a to 32 h are provided at equal intervals along the inner periphery of the bottom of the digestion tank body 1. Here, in the present embodiment, the discharge ports 33a to 33h of the branch press-fit pipes 32a to 32h have blades 2a whose liquid discharge directions from the discharge ports 33a to 33h rotate in the horizontal direction of the stirrer 2 in plan view. The direction is along the rotation direction r of (see FIG. 5).

  Moreover, the discharge direction of the liquid from the discharge ports 33a to 33h is a direction along the rotation direction r of the blade 2a rotating in the horizontal direction of the stirrer 2 and is further inclined downward with respect to the horizontal direction. .

  In addition, the discharge direction of the liquid from the discharge ports 33a to 33h may be a horizontal direction, not a diagonally downward direction with respect to the horizontal direction. Further, the liquid discharge direction from the discharge ports 33a to 33h is not a direction along the rotation direction r of the blade 2a of the stirrer 2, but is a direction toward the center of the digestion tank body 1 in a plan view, In a side view, the direction may be a direction obliquely downward with respect to the horizontal direction (in other words, a direction toward the center of the bottom of the digestion tank body 1).

(Discharge device)
The discharge device 7 of the present embodiment has a discharge pump 13 and one end connected to the discharge pump 13, and a suction port 20 a that is the other end is disposed in the digestion tank body 1 and below the blade 2 a of the stirrer 2. The discharge pipe 20 is made up of. The suction port 20a opens downward at the center of the bottom of the digestion tank body 1.

(Removal of sediment accumulated at the bottom of the digestion tank body)
First, the liquid supply pump 11 is operated to press-fit liquid from the branch press-fit pipes 32 a to 32 h into the bottom of the digestion tank body 1. The deposit S accumulated at the bottom of the digestion tank main body 1 migrates to the liquid phase portion in the digestion tank main body 1 by spraying the liquid from the liquid supply pump 11.

  In the present embodiment, the liquid is supplied from a plurality of locations near the inner peripheral wall of the bottom portion in the digestion tank body 1 in a direction obliquely downward with respect to the horizontal direction and along the rotational direction r of the blade 2a of the agitator 2. Since the particles are ejected, the migrated deposit S is easily collected at the center in the digestion tank body 1.

  Thereafter, the discharge pump 13 is operated to suck the sediment S collected in the center of the digestion tank body 1 from the discharge pipe 20 together with the fermentation liquid (sludge) in the digestion tank body 1 and discharge it outside the tank.

(Action / Effect)
The flow of the fermented liquid (sludge) due to the rotation of the blade 2a of the stirrer 2 is indicated by an arrow in FIG. As shown in FIG. 4, the rotation of the blade 2 a of the stirrer 2 generates a vertical flow f <b> 2 and a horizontal flow f <b> 1 in the digestion tank body 1. Since the flow f2 in the vertical direction is a flow that rises after spreading outward from the lower side of the blade 2a of the stirrer 2, the flow rate tends to be small at the bottom center in the digestion tank body 1 below the blade 2a. It is a part that tends to accumulate.

  Here, in the present embodiment, the digestion tank body 1 in the digestion tank body 1 in a direction obliquely downward with respect to the horizontal direction from a plurality of locations near the inner peripheral wall of the bottom portion in the digestion tank body 1 (the end of the bottom portion in the digestion tank body 1). The liquid is pressed into the tank, and the deposit S is discharged from the bottom of the blade 2a of the stirrer 2 to the outside of the tank by the discharge means. According to this configuration, the liquid is ejected from the end of the bottom portion in the digestion tank body 1 into the digestion tank body 1 in a direction obliquely downward with respect to the horizontal direction, whereby the digestion tank body 1 in which the deposits S easily accumulate. The deposit S tends to gather at the center of the bottom inside. Thereby, it becomes easy to discharge the deposit S from the suction port 20a to the outside of the suction tank.

  Moreover, in this embodiment, the liquid is ejected from the edge part of the bottom part in the digestion tank main body 1 toward the direction along the rotation direction r of the blade | wing 2a rotated in the horizontal direction of the stirrer 2. As shown in FIG. According to this configuration, the sediment S more easily collects at the bottom center in the digestion tank body 1 due to a synergistic effect with the horizontal flow f1 (rotating flow) generated by the rotation of the blade 2a of the stirrer 2.

  As described above, the direction in which the liquid is discharged from the discharge ports 33a to 33h is not the direction along the rotation direction r of the blade 2a of the stirrer 2, but the direction toward the center of the bottom of the digester tank body 1 It is good. In order to migrate and collect the sediment S to the bottom center in the digestion tank body 1, the liquid is ejected from the vicinity of the inner peripheral wall of the bottom in the digestion tank body 1 in a direction obliquely downward with respect to the horizontal direction. Is a common technical matter.

1: Digestion tank body (methane fermentation tank body)
2: Stirrer 3: Liquid press-fitting device (liquid press-fitting means)
4: Discharge device (discharge means)
5: Heating device (heating means)
11: liquid supply pump 12: press-fit liquid pipe 13: discharge pump 14: discharge pipe 15: circulation pump 16: warmer 21: discharge header pipes 22a-22g: branch press-fit pipes 23a-23g: discharge port 24 of the branch press-fit pipe : Suction header pipes 25a to 25g: Branch suction pipes 26a to 26g: Suction port of the branch suction pipe 100: Digestion tank (methane fermentation tank)

Claims (15)

A methane fermenter body,
Liquid press-fitting means for press-fitting liquid into the bottom of the methane fermentation tank body;
Discharging means for discharging the deposit deposited on the bottom of the methane fermentation tank main body to the outside of the tank;
With
The liquid press-fitting means includes
A liquid supply pump;
A press-fit liquid pipe connected to the liquid supply pump;
The press-fit liquid pipe is
A discharge header pipe connected to the liquid supply pump;
A plurality of branch press-fit pipes connected to the discharge header pipe,
The discharge direction of the liquid from the outlet of the branch press-fit pipe disposed at the end of the bottom in the methane fermentation tank main body is obliquely above the bottom surface of the methane fermentation tank main body, and the methane fermentation tank It is supposed to be in the direction toward the center of the main body,
A methane fermentation tank in which the deposit is migrated with the liquid injected from the liquid injection means, and the migrated deposit is discharged out of the tank by the discharge means. In the methane fermenter according to claim 1 ,
A discharge port of the branch press-fit pipe is also provided at the bottom center in the methane fermentation tank main body, and the liquid discharge direction from the discharge port is a direction toward the top plate of the methane fermentation tank main body. A methane fermenter. A methane fermenter body,
Liquid press-fitting means for press-fitting liquid into the bottom of the methane fermentation tank body;
Discharging means for discharging the deposit deposited on the bottom of the methane fermentation tank main body to the outside of the tank;
With
The liquid press-fitting means includes
A liquid supply pump;
A press-fit liquid pipe connected to the liquid supply pump;
There is only one press-fitting liquid pipe, one end of the press-fitting liquid pipe is connected to the liquid supply pump, and the other outlet is provided at the bottom center in the methane fermentation tank body. The discharge direction of the liquid from the discharge port is the direction toward the top plate of the methane fermentation tank body,
A methane fermentation tank in which the deposit is migrated with the liquid injected from the liquid injection means, and the migrated deposit is discharged out of the tank by the discharge means. In the methane fermenter in any one of Claims 1-3 ,
The discharging means is
A discharge pump;
A discharge pipe connected to the discharge pump;
A methane fermenter. In the methane fermenter according to claim 4 ,
The discharge pipe is
A suction header pipe connected to the discharge pump;
A plurality of branch suction pipes connected to the suction header pipe;
Have
The methane fermentation tank in which the inlets of the said some branch suction pipe are arrange | positioned along the side wall part of the bottom part in the said methane fermentation tank main body. In the methane fermenter according to claim 5 ,
The methane fermentation tank in which the inlet of the said branch suction pipe is arrange | positioned also in the bottom center in the said methane fermentation tank main body. A methane fermenter body,
Liquid press-fitting means for press-fitting liquid into the bottom of the methane fermentation tank body;
Discharging means for discharging the deposit deposited on the bottom of the methane fermentation tank main body to the outside of the tank;
With
The liquid press-fitting means includes
A liquid supply pump;
A press-fit liquid pipe connected to the liquid supply pump;
Inside the methane fermentation tank body, a stirrer for stirring the input organic waste is disposed,
The press-fit liquid pipe is
A discharge header pipe connected to the liquid supply pump;
A plurality of branch press-fit pipes connected to the discharge header pipe,
The discharge direction of the liquid from the discharge port of the branch press-fit pipe disposed at the end of the bottom in the methane fermentation tank body is a direction obliquely downward with respect to the horizontal direction,
The discharging means is
A discharge pump;
One end is connected to the discharge pump, and the other end of the suction port is disposed in the methane fermentation tank main body and below the blades of the stirrer, and
A methane fermentation tank in which the deposit is migrated with the liquid injected from the liquid injection means, and the migrated deposit is discharged out of the tank by the discharge means. In the methane fermenter according to claim 7 ,
The methane fermentation tank in which the discharge direction of the liquid from the discharge port of the branch press-fit pipe is further set to a direction along the rotation direction of the blades rotating in the horizontal direction of the stirrer. From the end of the bottom of the methane fermentation tank main body, obliquely above the bottom surface of the methane fermentation tank main body, and deposited on the bottom by press-fitting liquid toward the center of the methane fermentation tank main body A method for removing deposits in a methane fermentation tank, wherein deposits are migrated and the migrated deposits are discharged to the outside by a discharge means. By depositing liquid from the center of the bottom of the methane fermentation tank body toward the top plate of the methane fermentation tank body , the sediment deposited on the bottom part migrates, and the migrated deposit is removed from the tank by the discharge means. To remove sediment in the methane fermentation tank. In the deposit removal method in the methane fermentation tank according to claim 9 ,
The deposit removal method in a methane fermentation tank which press-fits a liquid also from the center of the bottom part in the said methane fermentation tank main body toward the top plate part of the said methane fermentation tank main body. In the deposit removal method in the methane fermentation tank in any one of Claims 9-11 ,
The deposit removal method in a methane fermentation tank which discharge | emits the said deposit to the outside of a tank by the discharge means from the several places along the side wall part of the bottom part in the said methane fermentation tank main body. In the deposit removal method in the methane fermentation tank in any one of Claims 9-12 ,
The deposit removal method in a methane fermentation tank which discharge | emits the said deposit to the outside of a tank by a discharge means from the center of the bottom part in the said methane fermentation tank main body. Inside the methane fermentation tank body, a stirrer that stirs the organic waste that has been put in is placed.
From the end portion of the bottom portion of the methane fermentation tank body, it was run the methane fermentation tank sediments deposited on the bottom by press-fitting the liquid into the body in an oblique downward direction to the horizontal direction, of the stirrer The deposit removal method in a methane fermentation tank which discharge | emits the deposit which migrated from the downward direction of a blade | wing to the tank outside by a discharge means. In the deposit removal method in the methane fermenter according to claim 14 ,
The deposit removal method in a methane fermenter which press-fits a liquid toward the direction along the rotation direction of the blade | wing rotated in the horizontal direction of the said stirrer from the edge part of the bottom part in the said methane fermenter main body.

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