JP2013010072A - Treatment method and treatment apparatus for organic waste - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a treatment method and a treatment apparatus for organic waste, allowing stable continuous-type thermal solubilization treatment by suppressing closing of a pressure regulating valve by thermally solubilized sludge.SOLUTION: This treatment apparatus 1 for the organic waste includes: a digestion tank 2 performing anaerobic digestion treatment of the organic waste W1; a dewatering device 7 performing dewatering treatment of the digestion-treated sludge performed with the anaerobic digestion treatment in the digestion tank 2; and a thermal solubilization tank 3 pressure-regulating organic waste W2 continuously put in from the digestion tank 2 by the pressure regulating valve 3A, performing the thermal solubilization treatment, and returning the thermally solubilized sludge M to the digestion tank 2. The treatment apparatus 1 for the organic waste includes, in at least one flow passage of a first flow passage S1 and a second flow passage S2, a small solid matter passage means 8 making only small solid matter having a size less than a maximum interval between a valve element and a valve seat in a maximum opening of the pressure regulating valve 3A of solid matter of the organic waste flowing in without being performed with the dewatering treatment flow downstream. The small solid matter passage means 8 comprises a strainer 9, for example.

Description

  The present invention relates to a processing method and a processing apparatus for anaerobic digestion treatment of organic waste.

  Anaerobic digestion treatment using anaerobic organisms can be used as a method for treating organic waste such as food waste (food waste), livestock manure and sewage sludge. This anaerobic digestion treatment generally heats the organic waste charged in the anaerobic digestion tank to a predetermined temperature and adjusts the hydrogen ion index (pH) of the organic waste to a predetermined pH value. Done. As a result, the organic waste undergoes methane fermentation through solubilization, hydrolysis, and acid fermentation, the solid content in the organic waste is decomposed into methane gas and carbon dioxide, and the solid content is reduced.

  Conventionally, a so-called heat solubilization treatment is performed in which organic waste is heated to a predetermined temperature in a heat solubilization tank (also referred to as a heat solubilization reactor) to hydrolyze the solid content. A method of introducing solubilized sludge into an anaerobic digester is known. For example, in Patent Document 1, high-temperature steam is supplied into a heat-solubilizing tank having a pressure regulating valve for adjusting pressure, and organic waste is supplied into a high-temperature / high-pressure heat-solubilizing tank. And techniques for heat solubilization are described. Patent Document 2 describes a technique in which a heat exchanger is provided in the heat solubilization tank, and the organic waste charged in the heat solubilization tank is heated by the heat exchanger to be heat solubilized. Yes.

Special table 2003-500208 JP 2008-296192 A

  However, since the treatment method described in Patent Document 1 is a batch system that discharges heat-solubilized sludge from the heat-solubilization tank and discharges high-temperature steam in the heat-solubilization tank, the following organic waste In order to heat solubilize, it is necessary to supply high temperature steam anew in the heat solubilization tank. That is, according to this batch method, every time organic waste is introduced into the heat solubilization tank, high temperature steam is required and a considerable amount of heat energy is required.

  Therefore, as a measure to reduce the heat energy in the heat solubilization treatment, the supply of crushed solids and the discharge of the heat solubilized sludge are carried out while the steam supplied in the heat solubilization tank is retained instead of the batch method. A continuous heat solubilization treatment can be considered. However, in the continuous heat solubilization treatment, the solid matter of organic waste may clog the pressure adjustment valve of the heat solubilization tank. In this case, the inside of the heat solubilization tank may be controlled to a predetermined pressure. It becomes difficult. For this reason, in the conventional heat solubilization treatment, a batch-type heat solubilization tank that can be released exclusively is used so that the sludge clogged in the pressure adjustment valve of the heat solubilization tank can be removed. Is real.

  On the other hand, in the technique using a heat exchanger instead of the high-temperature steam described in Patent Document 2, there is a problem that the solid content of organic waste is burnt on the surface of the heat exchanger, and the heat exchange rate is likely to decrease. . In addition, in order to avoid a decrease in the heat exchange rate, an operation such as removing the scale on the surface of the heat exchanger is necessary, which makes it difficult to manage.

  The present invention was devised to solve these problems, and is an organic waste that suppresses clogging of the pressure regulating valve due to heat-solubilized sludge and enables stable and continuous heat-solubilization treatment. An object of the present invention is to provide a processing method and a processing apparatus.

In order to solve the above problems, the present invention provides a digestion step for anaerobic digestion treatment of organic waste, a dehydration step for dehydration digestion-treated sludge subjected to anaerobic digestion in the digestion step, and the digestion step. The organic waste obtained from the digestion process was adjusted with a pressure regulating valve provided downstream, and continuously added to heat-solubilize it. A heat solubilization step for returning to the digestion step, and a method for treating organic waste, wherein the organic waste sent from the first flow path and the digestion step until the organic waste is input to the digestion step In at least one of the second flow paths until the organic waste is introduced into the heat solubilization step, the valve body at the maximum opening of the pressure regulating valve among the solids of organic waste Small solids less than the maximum distance between the valve seats Only a small solid passage means for flowing downstream provided, and wherein the flowing a organic waste in said small solid passing means without performing dehydration treatment.
Furthermore, a digester tank for anaerobically digesting organic waste, a dehydrator for dewatering digested sludge that has been anaerobically digested in the digester tank, and digested sludge drawn from the digester tank or the digester tank The organic waste that is continuously charged from the digested sludge storage tank is temporarily heat-solubilized after adjusting the pressure by a pressure regulating valve provided downstream, and the treated heat-solubilized sludge is treated as described above. An organic waste processing apparatus having a heat solubilization tank returned to the digestion tank, wherein the organic waste sent from the first flow path and the digestion tank until the organic waste is put into the digestion tank Organic waste that flows into the first flow path or the second flow path without being dehydrated in at least one of the second flow paths until the waste is put into the heat solubilization tank Of the pressure regulating valve Characterized in that a small solid passing means for passing only the size of the small solids downstream of less than the maximum distance between the valve body and the valve seat at the time of opening.

  Of the organic waste solids that flow in the slurry state, only small solids with a size less than the maximum distance between the valve body and the valve seat at the maximum opening of the pressure adjustment valve of the heat solubilization tank The clogging in the pressure regulating valve can be suppressed by providing the small solid material passage means for flowing the gas downstream. Therefore, in the heat solubilization tank, the organic waste can be subjected to heat solubilization treatment stably and continuously while retaining high-temperature steam. Since heat solubilization treatment is performed while hot steam is retained, the heat solubilization sludge is intermittently discharged as in the conventional heat solubilization treatment, and at the same time as the heat solubilization sludge is discharged, Almost all of the steam is discharged, and it is not necessary to supply organic waste to be heat-solubilized in the heat-solubilization tank and then supply high-temperature steam to the heat-solubilization tank. Thermal energy can be reduced and thermal efficiency can be improved. In addition, since no heat exchanger is used in the heat solubilization process, organic waste does not scorch the surface of the heat exchanger, eliminating the need for scale removal and facilitating maintenance.

  As another method of flowing only small solids into the heat solubilization tank, for example, organic waste is dehydrated and solidified once, and then crushed into small solids by a crushing device and heat solubilized tank The method of flowing in can be considered. However, since this method crushes highly concentrated solid content, the crushing resistance in the crushing apparatus increases, and an expensive crushing apparatus with a large driving force is required. In contrast, according to the present invention, the organic waste is allowed to flow into the small solid material passage means in a slurry state to obtain the small solid material, so that the structure is simple and economical.

  Further, the present invention is characterized in that the small solid material passing means comprises a crushing pump.

  By constructing the small solids passage means from a crushing pump, the solids of organic waste can be made into small solids with a size less than the maximum distance between the valve body and the valve seat when the pressure regulating valve is at the maximum opening. It can be crushed into objects. Since the crushing pump has a structure for crushing solids contained in slurry-like organic waste, crushing resistance is small. Therefore, the processing apparatus can be realized with a relatively inexpensive crushing pump having a small driving force.

  Further, the present invention is characterized in that the small solid material passing means is composed of a strainer or a screen.

  By constructing the small solids passage means from a strainer or a screen, it becomes a simple structure in which the organic waste in a slurry state is simply filtered by the strainer or the screen, and an economical processing apparatus can be realized.

  ADVANTAGE OF THE INVENTION According to this invention, the obstruction | occlusion in the pressure control valve of a heat solubilization tank is suppressed, and it becomes the processing method and processing apparatus of the organic waste which can perform the heat solubilization process of the stable continuous system.

It is a figure which shows the whole structure of the processing apparatus which concerns on 1st Embodiment of this invention. It is a figure which shows the whole structure of the processing apparatus which concerns on 2nd Embodiment of this invention. It is a figure which shows the whole structure of the processing apparatus which concerns on 3rd Embodiment of this invention. It is a figure which shows the whole structure of the processing apparatus which concerns on 4th Embodiment of this invention. It is a figure which shows the whole structure of the processing apparatus which concerns on 5th Embodiment of this invention. It is a figure which shows the whole structure of the processing apparatus which concerns on 6th Embodiment of this invention. It is a figure which shows an example of the crushing pump used by this invention, and is a sectional side view of the principal part. It is a figure which shows an example of the crushing pump used by this invention, and is an exploded perspective view of the principal part.

“First Embodiment”
In FIG. 1, a processing apparatus 1 includes a digestion tank 2 that performs anaerobic digestion treatment of organic waste W1, a dehydration apparatus 7 that performs a dehydration process on digestion-treated sludge that has been anaerobically digested in the digestion tank 2, and a digestion tank 2 Or the organic waste W2 continuously fed from the digested sludge storage tank (not shown) for temporarily storing the digested sludge extracted from the digestion tank 2 was pressure-adjusted by the pressure adjusting valve 3A interposed downstream. A heat solubilization tank (also referred to as a heat solubilization reactor) 3 that performs heat solubilization treatment and returns the treated heat solubilized sludge M to the digestion tank 2 is provided. Here, the flow path until the organic waste W1 is put into the digestion tank 2 is the first flow path S1, until the organic waste W2 sent from the digestion tank 2 is put into the heat solubilization tank 3. This flow path is referred to as a second flow path S2. In the second flow path S2, the flow path of the organic waste W2 from the digestion tank 2 to the heat solubilization tank 3 is provided even when the digested sludge storage tank (not shown) is provided in the middle. The second flow path S2 is assumed. The organic waste W1 is, for example, organic sludge such as sewage sludge and septic tank sludge, food waste, food waste, livestock manure, and the like.

The digestion tank 2 constitutes a digestion process for anaerobically digesting the organic waste W1. The digestion tank 2 causes the organic waste W1 to undergo methane fermentation (digestion treatment) with anaerobic methane fermentation bacteria. Methane-fermenting bacteria include hydrogen-utilizing methanogens that convert H ₂ to CH ₄ . Along with the methane fermentation, a digestion gas G mainly composed of CH ₄ and CO ₂ is generated from the digester ₂ , and all or a part thereof is sent to the boiler 4. The boiler 4 generates high-temperature steam by using the digestion gas G as fuel, and supplies it to the heat solubilization tank 3 as described later.

  The operating temperature of the digester 2 is appropriately set in consideration of the type of methane fermentation bacteria, doubling time, etc., but in the range tested by the present inventors, the operating temperature is 30 to 42 ° C. or 50 to 60 ° C. In this case, good results are obtained in terms of the amount of methane generated. In particular, better results are obtained when the temperature range is 35 to 38 ° C. in the former temperature range and 52 to 56 ° C. in the latter temperature range.

  The digestion tank 2 includes, for example, a stirrer 5 that stirs the organic waste in the tank. The stirrer 5 makes the temperature distribution of the organic waste uniform and promotes the digestion process. The structure of the stirring device 5 is not particularly limited. In FIG. 1, the stirring device 5 is rotated by a draft tube 5 </ b> A that is cylindrical and surrounds the central portion of the digester 2 and a drive device (not shown). The thing of the structure provided with the stirring blade 5B driven is illustrated. According to the stirring device 5, when the stirring blade 5B rotates, for example, a downward flow from the upper side to the lower side is generated inside the draft tube 5A, and an upward flow from the lower side to the upper side is generated outside the draft tube 5A. By doing so, the organic waste is effectively stirred in the entire digestion tank 2, and the uniform temperature distribution of the organic waste is promoted.

  The bottom of the digestion tank 2 is connected to a discharge path S4 for discharging organic waste as having been subjected to anaerobic digestion treatment. A dehydrator 7 is interposed in the discharge path S4, and a pump is provided upstream of the dehydrator 7. P2 is interposed. The dehydrator 7 constitutes a dehydration process for dehydrating the digested sludge that has been anaerobically digested in the digester 2. The dehydrator 7 is composed of, for example, a centrifugal dehydrator (decanter), a screw squeezing dehydrator, or the like. The digested sludge is dehydrated by the dehydrator 7 and processed as a dehydrated cake in a separate process. The dehydrated filtrate is sent to a water treatment system (not shown).

  The heat solubilization tank 3 heat-solubilizes the organic waste W2 continuously fed from the digestion tank 2 or a digested sludge storage tank (not shown), and the treated heat-solubilized sludge M passes through the reflux path S3. The heat solubilization process which returns to the digestion process which consists of the digestion tank 2 is comprised. The heat solubilization tank 3 is a device for heat solubilizing the organic waste W2 under conditions of high temperature and high pressure, and wastes steam when supplying the organic waste W2 and discharging the heat solubilized sludge M. It is a continuous-type heat solubilizing device that retains without discharging. The heat solubilization tank 3 includes a container 3B into which the organic waste W2 is charged, and a pressure adjustment valve 3A that is interposed in a flow path on the downstream side of the container 3B and controls the pressure in the container 3B. The opening degree of the pressure adjusting valve 3A is controlled for the purpose of adjusting the atmospheric pressure in the container 3B.

  Here, the pressure set in the heat solubilization tank 3 (container 3B) is approximately 0.2 MPa to 1.0 MPa, preferably 0.5 MPa to 0.8 MPa, and the set temperature is 120 ° C. to 180 ° C., Preferably it is 150 to 170 degreeC. The control unit (not shown) of the heat solubilization tank 3 is set to the set pressure and set temperature based on the temperature and pressure in the container 3B measured by a temperature sensor and a pressure sensor (both not shown). In addition, a steam valve (not shown) interposed in the flow path with the boiler 4 and the pressure regulating valve 3A are controlled to open and close.

  The second flow path S2 is provided with a dehydrating device 6 for dehydrating the organic waste W2 that has been anaerobically digested in the digesting tank 2 and flowing it to the heat solubilizing tank 3, and upstream of the dehydrating apparatus 6. A pressure feed pump P1 is interposed on the side. Similarly to the dehydrator 7, the dehydrator 6 includes a centrifugal dehydrator (decanter), a screw press dehydrator, and the like. The dehydrated filtrate discharged from the dehydrator 6 is sent to a water treatment system (not shown).

  In the processing apparatus 1 described above, the present invention relates to organic waste that flows in a slurry state in at least one of the first flow path S1 and the second flow path S2 (in the case of the first flow path S1). Is a small size less than the maximum distance between the valve body and the valve seat at the time of the maximum opening degree of the pressure regulating valve 3A among the solid materials of the second flow path S2) The main feature is that a small solid material passage means 8 for flowing only solid materials downstream is provided, and the organic waste W1 or W2 is allowed to flow into the small solid material passage means 8 without dehydration. In other words, the organic waste W1 is not dehydrated upstream of the small solids passage means 8 provided in the first flow path S1, and the organic waste W2 from the digestion tank 2 to the second flow path S2. The dehydration process is not performed until the small solids passing means 8 provided in FIG. Of course, since the dehydrating device 6 is located downstream of the small solids passing means 8, it does not correspond to the dehydrating process from the digester 2 to the small solids passing means 8.

  The size of the small solid matter is related to the width of the throttle passage formed by the distance between the valve body of the pressure regulating valve 3A of the heat solubilization tank 3 and the valve seat on which the valve body can be seated. Specifically, the size of the small solid is a value less than the maximum distance between the valve body and the valve seat of the pressure regulating valve 3A at the maximum opening. Note that the maximum distance is, for example, the width of the annular throttle passage between the valve body and the valve seat when an annular throttle passage is formed by the valve body and the valve seat. Equivalent to. More preferably, the supply of the organic waste W2 to the heat solubilization tank 3 and the heat solubilization tank in a state where the steam supplied in the heat solubilization tank 3 is retained with the opening of the pressure regulating valve 3A. It is set to be equal to or smaller than the width of the throttle passage when the opening is such that the heat-solubilized sludge M can be discharged from 3. For this purpose, the small solids passage means 8 allows only small solids having a size of, for example, 2 mm or less, more preferably 1 mm or less, to flow downstream.

In the present embodiment, the small solids passage means 8 is constituted by a strainer 9 provided in the second flow path S2. The strainer 9 is provided upstream of the dehydrator 6. Further, in addition to the strainer 9 provided in the second flow path S2, a screen 10 may be provided as the small solid material passing means 8 also in the first flow path S1. The strainer 9 includes, for example, a cylindrical filter medium in which filtration holes are formed in a mesh shape or a lattice shape. The bucket type captures large solids by the filter medium and flows only small solids less than the filter holes downstream. A known structure such as a strainer is applied. The slurry-like organic waste W2 flowing through the second flow path S2 is removed by the strainer 9 from the solid material having a size larger than the maximum distance between the valve body and the valve seat when the pressure regulating valve 3A is at the maximum opening degree. Then, it flows to the dehydrator 6. The large solid matter captured by the strainer 9 is sent to, for example, the discharge path S4 and processed by the dehydrator 7.
In addition, the dehydration apparatus 6 which consists of a centrifugal dehydrator (decanter), a screw squeezing type dehydrator, etc. has a function of flowing only small solids among large and small solids, a function of reducing the size of solids, and the like. It does not correspond to the small solids passage means 8.

  The organic wastes W1 and W2 are preferably passed through the small solids passage means 8 in a slurry state with a solids concentration of 2 to 15 Wt% (wt / wt), preferably 2 to 10 Wt% (wt / wt). . Paying particular attention to the organic waste W2 flowing through the second flow path S2, the dehydrator 6 is located downstream of the small solids passage means 8. The dehydrating device 6 is set so that the solid concentration in the dehydrated solid is 10 to 35 Wt% (wt / wt), preferably 15 to 25 Wt% (wt / wt). The solid concentration is set to at least 10 Wt% or more because when the solid content of the organic waste is heat-solubilized in the downstream heat-solubilization tank 3, the heat energy is deprived of moisture in the organic waste. This is to reduce the heat energy used in the heat solubilization step. On the other hand, the upper limit side of the solid concentration is set to 35 Wt% from the viewpoint of the smooth flow of the organic waste in the flow path. Thus, in order to make the solid concentration in the dehydrated solids easily 10 to 35 Wt% in the dehydrator 6, in the small solids passage means 8 provided on the upstream side of the dehydrator 6, organic waste is disposed. It is desirable that the solid matter concentration of the material W2 flows in as a slurry state of 2 to 15 Wt% (wt / wt), preferably 2 to 10 Wt% (wt / wt).

  Next, as the screen 10 provided in the first flow path S1, for example, a known bar screen in which a plurality of bars are arranged in parallel in the vertical direction or the horizontal direction can be applied. This bar screen captures large solids in the organic waste W1 flowing through the first flow path S1, and only the liquid component and small solids flow downstream from the opening between the bars and enter the digester 2. It is thrown. The width of the opening is, for example, 4 to 15 mm.

  According to the processing apparatus 1 of the present embodiment, the small solid material passing means 8 including at least the strainer 9 has a size less than the maximum distance between the valve body and the valve seat when the pressure regulating valve 3A is at the maximum opening degree. Since only small solids flow into the heat solubilization tank 3, clogging due to organic waste (specifically, heat solubilized sludge M) in the pressure regulating valve 3A can be suppressed. Therefore, in the heat solubilization tank 3, the organic waste W2 can be continuously heat-solubilized stably while the high-temperature steam is retained. Since heat solubilization treatment is performed while hot steam is retained, the heat solubilization sludge is intermittently discharged as in the conventional heat solubilization treatment, and at the same time as the heat solubilization sludge is discharged, Almost all of the steam is discharged, and it is not necessary to supply organic waste to be heat-solubilized in the heat-solubilization tank and then supply high-temperature steam to the heat-solubilization tank. Thermal energy can be reduced and thermal efficiency can be improved. In addition, since no heat exchanger is used in the heat solubilization process, organic waste does not scorch the surface of the heat exchanger, eliminating the need for scale removal and facilitating maintenance.

  Here, as another method of flowing only small solids having a size less than the maximum distance between the valve body and the valve seat at the time of the maximum opening of the pressure regulating valve 3A to the heat solubilization tank 3, for example, organic A method is conceivable in which the waste W1 or W2 is dehydrated and solidified once, and is crushed by a crushing device into small solids. However, since this method crushes highly concentrated solid content, the crushing resistance in the crushing device increases, and an expensive crushing device with a large driving force is required. On the other hand, according to the processing apparatus 1 of this embodiment, since it becomes a structure which only filters the organic waste W2 of a slurry state with the strainer 9, the structure is simple and can implement | achieve the economical processing apparatus 1. FIG.

“Second Embodiment”
The processing apparatus 1 of 2nd Embodiment is demonstrated with reference to FIG. In the second embodiment, the same components as those in the first embodiment are denoted by the same reference numerals, and the description thereof is omitted.
In the processing apparatus 1 of the second embodiment, a crushing pump 11 as a small solid material passing means 8 is provided in the first flow path S1, and a strainer 9 or a screen as the small solid material passing means 8 is provided in the second flow path S2. 10 is provided.

  In the first flow path S1, the organic waste W1 is first charged into the raw material storage tank 12. Near the bottom of the raw material storage tank 12 and the inlet of the crushing pump 11 are connected via a flow path T1. The flow path connected to the discharge port of the crushing pump 11 branches in the middle, one flow path T2 is connected to the upper part of the raw material storage tank 12, and the other flow path T3 is connected to the digestion tank 2. Open / close valves V1, V2 are interposed in the flow paths T2, T3, respectively.

  For example, as shown in FIGS. 7 and 8, the crushing pump 11 includes a fixed cutting blade 13 whose tip (lower end) is formed as a straight blade, an axial flow type crushing impeller 14, and a crushing impeller. 14, a shroud ring 15 attached to the outside, a lattice member 16 attached to the downstream side of the crushing impeller 14, and a pressure impeller 17 provided on the downstream side of the lattice member 16. In FIG. 2, the solid matter of the organic waste W1 flowing into the crushing pump 11 from the raw material storage tank 12 through the flow path T1 is first upstream of the crushing impeller 14 that rotates with the cutting blade 13 in FIGS. Roughly cut by the edges. Next, the solid matter is agitated and fed by the crushing impeller 14, and at this time, a part of the solid strikes the blade portion of the shroud ring 15 and is cut by the centrifugal force. Further, the solid matter is further finely crushed (crushed) between the crushing impeller 14 and the lattice-like member 16, and after being pressurized by the pressure impeller 17, it is discharged to the outside from the discharge port. About the size of the solid matter discharged from the discharge port, for example, by appropriately setting the number of blades of the crushing impeller 14, the size of the lattice of the lattice member 16, the flow velocity, etc. 2 can be set to a size smaller than the maximum distance between the valve body and the valve seat when the pressure regulating valve 3A shown in FIG.

  The organic waste W1 flows into the crushing pump 11 from the raw material storage tank 12 in a slurry state with a solid concentration of 2 to 15 Wt% (wt / wt), preferably 2 to 10 Wt% (wt / wt). When the organic waste W1 is crushed by the crushing pump 11, the open / close valve V1 is opened to connect the flow path T2, the open / close valve V2 is closed to close the flow path T3, the raw material storage tank 12 and the crush pump The organic waste W1 is circulated for a predetermined time with the crushed material 11 and crushed. Then, after the crushing process, the on-off valve V1 is closed to close the flow path T2, and the open / close valve V2 is opened to bring the flow path T3 into communication so that a slurry-like organic waste containing only small solids is disposed. The thing W1 is thrown into the digestion tank 2. Therefore, also in the organic waste W2 sent out from the digestion tank 2, it is thrown into the heat solubilization tank 3 as a slurry state containing only small solids.

  According to the processing apparatus 1 of this embodiment, the solid matter in the organic waste W1 is removed by the small solids passage means 8 including the crushing pump 11 between the valve body and the valve seat when the pressure regulating valve 3A is at the maximum opening degree. It can be crushed into small solids with a size less than the maximum interval between them. Further, since the strainer 9 or the screen 10 is provided in the second flow path S2, clogging in the pressure regulating valve 3A can be further suppressed by these synergistic effects. Therefore, in the heat solubilization tank 3, the organic waste W2 can be continuously heat-solubilized stably while the high-temperature steam is retained.

  Moreover, according to the processing apparatus 1 of this embodiment, since the crushing pump 11 is the structure which crushes the solid substance contained in the organic waste W1 of a slurry state, crushing resistance may be small. Therefore, the processing apparatus 1 can be realized by a relatively inexpensive crushing pump 11 having a small driving force.

“Third Embodiment”
The processing apparatus 1 of 3rd Embodiment is demonstrated with reference to FIG. In the third embodiment, the same components as those of the second embodiment are denoted by the same reference numerals, and the description thereof is omitted.
The processing apparatus 1 of 3rd Embodiment is provided with the crushing pump 11 and the strainer 9 or the screen 10 as the small solid substance passage means 8 in 1st flow path S1. FIG. 3 shows an example in which the crushing pump 11 is arranged on the upstream side, and the strainer 9 or the screen 10 is arranged on the downstream side.

  According to the processing apparatus 1 of this embodiment, the size of the solid matter in the organic waste W1 by the crushing pump 11 is less than the maximum distance between the valve body and the valve seat when the pressure regulating valve 3A is at the maximum opening degree. The clogging in the pressure regulating valve 3A can be further suppressed by the synergistic effect with the strainer 9 or the screen 10. Therefore, in the heat solubilization tank 3, the organic waste W2 can be continuously heat-solubilized stably while the high-temperature steam is retained.

“Fourth Embodiment”
The processing apparatus 1 of 4th Embodiment is demonstrated with reference to FIG. In the fourth embodiment, the same components as those in the third embodiment are denoted by the same reference numerals, and the description thereof is omitted.
In the processing apparatus 1 of the fourth embodiment, a strainer 9 or a screen 10 is provided as the small solids passage means 8 in the first flow path S1. A raw material storage tank 12 is provided on the upstream side of the strainer 9 or the screen 10. A pressure feed pump P <b> 3 is provided between the strainer 9 or screen 10 and the raw material storage tank 12.

  According to the processing apparatus 1 of the present embodiment, only the small solid matter having a size less than the maximum distance between the valve body and the valve seat at the time of the maximum opening of the pressure regulating valve 3A is heated by the strainer 9 or the screen 10. Since it flows into the solubilization tank 3, clogging in the pressure regulating valve 3A can be suppressed. Therefore, in the heat solubilization tank 3, the organic waste W2 can be continuously heat-solubilized stably while the high-temperature steam is retained.

“Fifth Embodiment”
The processing apparatus 1 of 5th Embodiment is demonstrated with reference to FIG. In the fifth embodiment, the same components as those in the second embodiment are denoted by the same reference numerals, and the description thereof is omitted.
The processing apparatus 1 of 5th Embodiment is provided with the crushing pump 11 as the small solid substance passage means 8 on the upstream side of the dehydrating apparatus 6 in the second flow path S2.

  According to the processing apparatus 1 of the present embodiment, only the small solid matter having a size less than the maximum distance between the valve body and the valve seat at the time of the maximum opening of the pressure regulating valve 3A is thermally solubilized by the crushing pump 11. Since it flows into the tank 3, clogging in the pressure regulating valve 3A can be suppressed. Therefore, in the heat solubilization tank 3, the organic waste W2 can be continuously heat-solubilized stably while the high-temperature steam is retained.

“Sixth Embodiment”
The processing apparatus 1 of 6th Embodiment is demonstrated with reference to FIG. In the sixth embodiment, the same components as those in the fifth embodiment are denoted by the same reference numerals, and the description thereof is omitted.
The processing apparatus 1 of 6th Embodiment is provided with the crushing pump 11 and the strainer 9 or the screen 10 as the small solid substance passage means 8 in the 2nd flow path S2 in the upstream of the dehydration apparatus 6. FIG. FIG. 6 shows an example in which the crushing pump 11 is provided on the upstream side of the strainer 9 or the screen 10.

  According to the processing apparatus 1 of the present embodiment, the solid matter in the organic waste W2 by the crushing pump 11 is smaller than the maximum distance between the valve body and the valve seat when the pressure regulating valve 3A is at the maximum opening degree. The clogging in the pressure regulating valve 3A can be further suppressed by the synergistic effect with the strainer 9 or the screen 10. Therefore, in the heat solubilization tank 3, the organic waste W2 can be continuously heat-solubilized stably while the high-temperature steam is retained.

  The preferred embodiments of the present invention have been described above. When the small solid material passage means 8 is provided only in the first flow path S1, the solid material reduced in size by the small solid material passage means 8 is entangled again in the digestion tank 2 to become a large solid material, and an organic material containing this. In view of the possibility that the waste W2 may flow into the heat solubilization tank 3, it is preferable that the small solid material passing means 8 is provided in at least the second flow path S2.

1 Processing device 2 Digestion tank (digestion process)
3 Heat solubilization tank (heat solubilization process)
3A Pressure regulating valve 7 Dehydrator (Dehydration process)
8 Small solids passage means 9 Strainer 10 Screen 11 Crushing pump 12 Raw material storage tank M Heat-solubilized sludge S1 1st flow path S2 2nd flow path W1, W2 Organic waste

Claims (6)

A digestion process for anaerobic digestion of organic waste;
A dehydration step of dehydrating the digested sludge that has been anaerobically digested in the digestion step;
The organic waste obtained through the digestion process in the digestion step is pressure-adjusted with a pressure regulating valve provided downstream, and then continuously charged and heat-solubilized. A heat solubilization step for returning solubilized sludge to the digestion step;
An organic waste processing method comprising:
At least one of the first channel until the organic waste is input to the digestion step and the second channel until the organic waste sent from the digestion step is input to the heat solubilization step In the flow path,
A small solids passage means is provided that allows only small solids having a size less than the maximum distance between the valve body and the valve seat at the maximum opening of the pressure regulating valve to flow downstream among the solids of organic waste. ,
A method for treating organic waste, wherein the organic waste is allowed to flow into the small solids passage means without being dehydrated.   The method for treating organic waste according to claim 1, wherein the small solids passage means comprises a crushing pump.   2. The method for treating organic waste according to claim 1, wherein the small solids passage means comprises a strainer or a screen. A digester for anaerobic digestion of organic waste;
A dehydrator for dehydrating digested sludge that has been anaerobically digested in the digestion tank;
The organic waste that is continuously introduced from the digestion tank or the digested sludge storage tank that temporarily stores the digested sludge drawn from the digestion tank can be heated after the pressure is adjusted by a pressure regulating valve provided downstream. A heat solubilization tank for solubilizing and returning the treated heat solubilized sludge to the digestion tank;
An organic waste processing apparatus having
At least one of the first flow path until the organic waste is put into the digestion tank and the second flow path until the organic waste sent from the digestion tank is put into the heat solubilization tank In the flow path,
The maximum distance between the valve body and the valve seat at the maximum opening of the pressure regulating valve among the organic waste solids flowing in without being dehydrated in the first flow path or the second flow path A processing apparatus for organic waste, characterized in that there is provided a small solids passage means for flowing only small solids having a size less than that downstream.   The organic waste processing apparatus according to claim 4, wherein the small solids passage means includes a crushing pump.   The organic waste processing apparatus according to claim 4, wherein the small solids passage means includes a strainer or a screen.

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