JP4415273B2 - Organic sludge treatment facility - Google Patents

Description

The present invention relates to an organic sludge treatment system and an organic sludge treatment facility , and more particularly, to an organic sludge treatment facility for treating a large amount of organic sludge.

  The recent sophistication of economy and social life has caused mass consumption and mass dumping, thereby causing environmental pollution and becoming a social problem. Examples of waste discharged by mass dumping include waste from business establishments, waste discharged by producers, livestock manure, food sludge, domestic waste discharged from households, and sewer sludge. Among these, food sludge, which accounts for a large proportion of general industrial waste, is a numerical value that is reused as raw material for fertilizer, etc., as a result of the recent revision of the law, in the process of production and processing It is positioned as the mission of the public with goals. In other words, considering the labor, time, and cost required for processing, organic sludge (organic waste discharged by food manufacturing companies, food waste discharged by dining companies, livestock manure, household waste discharged from households, and other food sludge) Is a problem that must be realized as soon as possible. About the processing method of organic sludge, various proposals are conventionally made like literatures 1 and 2.

JP 2002-35795 A JP 2005-74328 A

  The organic sludge treatment apparatus of Patent Document 1 has a filter cloth stretched in a dehydration chamber in a treatment tank, and a sludge dehydration treatment chamber is provided above and a dehydration filtrate chamber is provided below, and air is supplied to the dehydration treatment chamber. The filtrate chamber is partitioned into a plurality of air chambers, and each pressure air chamber is subjected to high-pressure air supply and filtrate discharge to reversely wash the filter cloth to prevent clogging. Further, in Patent Document 2, a high-temperature dry exhaust gas generated from a dryer in which a dewatered cake obtained by dehydrating organic sludge containing ammonia is dried in a distillation column that performs ammonia stripping of a separated liquid separated from organic sludge. By using it as a carrier gas, the processing equipment is made compact by eliminating the need for condensing means for dry exhaust gas and water treatment of the condensate. However, all of these conventional technologies are related to the treatment of organic waste within the facilities of a single operator. All of these conventional technologies accept various and large amounts of organic sludge and treat them daily. For example, it could not cope with organic sludge treatment that occurs in large quantities every day, for example, about 20 tons. In addition, the equipment cost and the operating cost are expensive, and there has been a difficulty in practical use of mass processing equipment.

The present invention has been made in view of the above-described conventional problems, and one object of the present invention is to reliably process organic waste generated in a large amount every day with a simple configuration, and to efficiently process it in a short time. Another object of the present invention is to provide an organic sludge treatment method and an organic sludge treatment facility that can be used as fertilizer.

In order to achieve the above object, the present invention includes a crushing and mixing unit 12 that mixes a powder in which microorganisms are implanted at a predetermined ratio with respect to organic sludge to be carried in, and crushes the powder to a required particle size. and organic sludge primary reservoir 14 for curing and accumulating while performing crosscut handle post fermentation processing unit 16 for fermentation treatment of organic sludge while supplying air containing the organic sludge after treatment in the primary reservoir 14 When having a fermentation process unit 16 includes a plurality of sealed chambers 18 that are features, the sealed chamber 18 includes a sealed chamber 181 to 1 88 organic sludge is turned stand, the enclosed chamber A heated air injection pipe 32 for injecting heated air into the input organic sludge, a suction / discharge section 34 for sucking and discharging air containing vapor generated by microbial fermentation of the organic sludge, and deodorizing the sucked gas Deodorizing part 36 In one site, the crushing and mixing unit 12 and the primary storage unit 14 are arranged as opposed to the central transport space 22 in the middle as a pretreatment unit, and the plurality of sealed processing chambers of the fermentation processing unit 16 are crushed and mixed. respectively adjacent juxtaposed parts 12 and primary reservoir 14, and are disposed on opposite positions arranged central transfer space 22 to the intermediate, sealed chamber 181-1 88 is at least two times or more carry-date amount of organic sludge, respectively It is composed of a treatment facility for organic sludge characterized in that eight or more are arranged in the volume.

At that time, the temperature of the heated air into the organic sludge put into the sealed chambers 181 to 190 is preferably 25 degrees to 35 degrees.

According to the organic sludge treatment facility of the present invention, a crushing and mixing unit for mixing the powder on which the microorganisms are implanted while crushing the organic sludge to be carried in, and the primary for storing and curing the organic sludge after crushing and mixing A storage unit and a fermentation processing unit for fermenting organic sludge supplied with air, and the fermentation processing unit includes a plurality of enclosed chamber devices, and the sealed chamber device is charged with organic sludge A closed chamber, a heated air injection pipe for injecting heated air into the organic sludge charged into the sealed chamber, and a suction exhaust for sucking and discharging air containing vapor generated by microbial fermentation of the organic sludge And a deodorizing part for deodorizing the sucked gas, and each sealed chamber has a volume that is at least twice as large as the amount of organic sludge carried in, and within 4 days including crushing mixing and primary storage Multiple pre-treatments and two-week closed-chamber fermentation Since the organic sludge corresponding to the input daily amount is processed every day by carrying out the chamber sequentially and continuously, the organic waste generated in large quantities every day with a simple configuration can be reliably processed and efficiently and in a short period of time. It can be processed and fertilized.

  In addition, the temperature of the heated air into the organic sludge charged into the sealed chamber is set to 25 to 35 degrees to promote the aerobic fermentation of the organic sludge to be treated by the aerobic microorganisms. Fermentation over time can be performed.

In addition, according to the organic sludge treatment method of the present invention, the step of mixing the powder on which the microorganisms are implanted while crushing the organic sludge, and storing the organic sludge after mixing and supplying air by a reversing operation The process, the step of introducing the organic sludge supplied with air into the sealed room and allowing it to stand still, then blowing the heated air continuously from the bottom of the room and injecting it into the organic sludge; Including a step of transpiration into the indoor air portion, a step of sucking and ventilating the gas in the sealed chamber together with the transpiration to the indoor air portion, and a step of deodorizing the sucked-in gas. In addition, because it is configured to perform organic sludge fermentation treatment equivalent to at least the same amount as the input of processing within 24 hours by sequential work, organic waste generated in large quantities every day can be reliably processed with a simple configuration, and Rate well treated short time, and this can be achieved that the fertilizer.

  Furthermore, the temperature of the heated air into the organic sludge in the sealed chamber is 25 to 35 degrees C., and the microbial fermentation promotes the fermentation after the primary fermentation step in which the internal temperature of the organic sludge rises to about 60 ° C. By including the secondary fermentation step at about 85 ° C., the aerobic fermentation of the organic sludge to be treated by the aerobic microorganism can be promoted, and the fermentation action can be performed in a short time under good conditions.

  The best mode for carrying out the present invention will be described below with reference to the accompanying drawings. The organic sludge treatment system and the organic sludge treatment method of the present invention provide a means for treating sewage sludge, domestic waste, livestock manure, food residue and other organic sludge, and in particular, a large amount of organic waste discharged daily. Disclosed is an organic sludge treatment system and method capable of reliably treating materials in a short period of time by installing them with simple facilities and in a relatively small space. The present system and method also treats organic waste discharged from food production factories, general business establishments, households, etc., livestock manure discharged from livestock feed farms, and other organic waste.

  1 to 3 show an organic sludge treatment system according to an embodiment of the present invention and an apparatus or facility for realizing the system, and in FIG. 1, the organic sludge treatment system crushes organic sludge. A crushing and mixing unit 12 that mixes the powder on which the microorganisms are implanted, a primary storage unit 14 that stores and cures the organic sludge after crushing and mixing, and a fermentation processing unit 16 that ferments the organic sludge supplied with air. The fermentation processing unit includes a plurality of sealed chamber devices 18 provided side by side.

  In the embodiment of FIG. 1, the short wall 201 and the long wall 202 are opposed to each other, a long rectangular outer wall is erected on the long rectangular site, and a roof 203 is installed on the upper end of the wall to form the processing facility 20. Has been. A transport lane 22 is provided in the lateral direction from one end to the other end in the center in the width direction of the floor of the processing facility 20, open doors 201a and 201b are provided in the left and right short walls 201, and the left short wall 201 is further provided. An entrance / exit 202a is formed in a part of the long side wall adjacent to.

  In the processing facility 20, the stock yard 24, the crushing and mixing unit 12, and the fermentation processing unit 16 a are arranged in order from the left rear side to the right side in FIG. The primary storage unit 14 is provided so as to be opposed to the crushing and mixing unit 12 and partitioned by the partition walls W3 and W4 with the conveyance lane 22 therebetween, and the fermentation processing unit 16b is disposed on the right side thereof. Further, a bagging processing unit 26 is provided adjacent to the fermentation processing units 16a and 16b.

  The sludge carried into the stockyard generally has a moisture content of about 80%. The crushing and mixing unit 12 is a part that mixes the powder in which microorganisms are implanted while crushing the organic sludge that is brought in from the outside and stored in the stock yard 24. From the hopper, the powder in which the microorganisms are deposited together with the organic sludge to be treated is introduced from the hopper, the sludge stuck in a lump is crushed, and the microbial powder is mixed with the organic sludge. The particle diameter of the sludge containing microorganisms passed through the mixing crusher is adjusted to about 5 mm particle diameter, for example. Microbial powder is, for example, a powder containing microorganisms by spraying a liquid in which primary cells obtained by culturing bacteria are spray-sprayed on zeolite, vermiculite, sawdust, etc. For example, the microbial powder is added to the sludge 10 at a weight ratio of about 1:10 and mixed and stirred. Powders containing microorganisms are prepared with a certain degree of humidity. Examples of the microorganism to be implanted include Streptococcus, Saccharomyces, Bacillus subtile, and Corynebacterium.

  The primary storage unit 14 is a primary storage means for storing and curing organic sludge after crushing and mixing. For example, the organic sludge after crushing and mixing is introduced into an interior having an upper surface opened and partitioned by a long rectangular wall. In addition, an air supply device for supplying air into the sludge by a reversing operation is provided so that the sludge is not spoiled using a stirring blade or other reversing device. The primary storage unit 14 performs primary storage and waits until the processing treatment sludge is carried into the fermentation processing unit 16 of the next process, and the sludge after mixing and stirring is stabilized and cured in a state that facilitates fermentation. The crushing and mixing unit 12 and the primary storage unit 14 constitute a pre-processing unit or a pre-processing step that waits for a required amount input time to the sealed chambers 181 to 188 while performing a pre-processing step before the fermentation process.

In FIG. 1, the fermentation processing unit 16 includes a plurality of sealed chamber devices 18 arranged in the same processing facility 20. That is, the first sealed chamber group Cm1 is installed so as to be successively adjacent to each other with the wall sandwiched between the crushing and mixing unit 12, and continuously adjacent to the sealed chamber group Cm1 with the transport lane 22 therebetween. A second sealed chamber group Cm2 is installed. The first sealed chamber group Cm1 has four sealed chambers 181 to 184 adjacent to each other across the walls W5 to W7, and the second sealed chamber group Cm2 also includes the walls W8 to W10 with the same side-by-side configuration. There are four adjacent sealed chambers 185 to 188 so as to be adjacent to each other. Each of the sealed chambers 181 to 188 has an opening / closing door 30 on the transfer lane 22 side, and is closed by a back wall Wb, an outer wall Wt, and a ceiling wall Wc so as to be kept airtight to some extent. .

  The sealed chambers 181 to 188 are closed and closed fermenters that are charged with organic sludge and allowed to stand for microbial fermentation. In the embodiment, each sealed chamber has a large capacity space. That is, each sealed chamber has a volume that is at least twice as large as the amount of organic sludge carried in. For example, if the daily amount carried into the stockyard 24 is 20 tons, each sealed chamber is configured to have a size that can accommodate, for example, 85 tons or more of sludge. Then, for example, 80 tons of processing target sludge to be put into the sealed chamber is stored in the primary storage unit 14 as a pretreatment process within about 4 days, and for example, 80 tons of sludge stored in each sealed chamber is stored at a time. It is thrown into the sealed room. That is, the sludge that is brought in every day is accumulated to the required amount within the capacity of each sealed room, and it is managed so as not to be spoiled during this time, and after the accumulation of the required amount is completed, the sludge is put into one sealed room at a time. This is done sequentially. This makes it possible to easily manage the fermentation of organic sludge in a sealed room and to reliably perform the treatment.

  1 to 3, the sealed chamber device 18 further includes a heated air injection pipe 32, a suction / discharge unit 34, and a deodorization unit 36. As shown in FIGS. 2 and 3, the heated air injection pipe 32 has, for example, a plurality of (for example, three) parallel grooves 38 formed in a concrete floor, and is embedded in each groove. It is composed of a metal tube having a large number of air ejection holes 40 formed on the outer periphery. From the air ejection hole 40, warm air of about room temperature, for example, about 25 ° C. to 35 ° C. is diffused toward the outside. Therefore, since the organic sludge to be treated is introduced into the sealed chamber and the heated air is ejected, the heated air is directly injected into the organic sludge. At this time, the heated air is injected from the injection pipe 32 into the organic sludge of the heated air with an injection pressure that reaches a distance of about 70% to 90% of the bulkiness of the organic sludge in the sealed chamber. As a result, the natural temperature rise due to microbial fermentation evaporates the water in the sludge and releases it to the residual air section 42 in the sealed chamber.

  As shown in FIGS. 1 and 2, a machine room 44 is installed on the back side of the sealed chambers 181 to 188, and heated air including a blower 46 and a heater 48 corresponding to each sealed chamber in the machine room 44. An injection driving device 49 is installed, and the heater 48 is connected in communication with the warmed air injection pipe 32 and the pipe 50 in the corresponding sealed chamber. Each blower 46 and heater 48 are electrically connected to a control device (not shown), and each device is turned on so that the difference between the room temperature detected by the temperature sensor 56 and the set room temperature falls within the set range. The closed room temperature is adjusted to an appropriate blown air volume and set temperature by turning off and adjusting the air volume and temperature. These adjustments may be performed manually by an operator, for example, at 25 ° C. to 35 ° C. by adjusting the desired blown air volume and temperature from the heated air injection pipe 32 by adjusting operations such as knobs. The heated air may be injected from the heated air injection pipe 32 into the sludge at the set ejection amount or speed.

  The suction discharge unit 34 is a suction discharge unit that sucks and discharges air containing vapor generated by microbial fermentation of organic sludge from the sealed chamber. In this embodiment, the suction fan is attached to the back wall Wb of each sealed chamber. 52. Further, a deodorizing device as a deodorizing unit 36 is provided outside the sealed chamber in communication with the suction fan 52, and the high-temperature air in the sealed chamber sucked and discharged by driving the suction fan is sent to the deodorizing device. The latter air is cooled to an intermediate temperature by a cooling device provided with a water jacket or the like, supplied to the blower side along with fresh air from the outside through a pipe leading to the blower 46, and again ejected from the heated air injection pipe 32 Then, it is refluxed, or it is treated by an appropriate method such as release of outside air. The deodorization device takes out odors by passing air containing steam generated from organic sludge in a sealed chamber through a tank filled with charcoal, bamboo charcoal, zeolite, sawdust, etc. in a plurality of layers.

  Then, within 4 days when the pretreatment is completed in each sealed chamber of the sealed chamber device 18, that is, in this embodiment, the crushing and mixing step and the primary storage step are used continuously for 4 days, and then sealed for 14 days continuously. A fermentation process is performed in the chambers 181 to 188. After the organic sludge is brought into each sealed room, injection of warm air into the organic sludge put into the sealed room is started, and this is carried out sequentially and continuously for all the sealed rooms, for example, every day. A large amount of organic sludge with a daily volume of about 20 tons can be reliably treated. As a result, about 20 tons of organic sludge can be transported and held in the processing facility every day, and the 20 tons of sludge can be reliably composted every day.

In this embodiment, this process is performed by eight sealed chamber devices, but each sealed chamber has a volume that is at least twice the daily amount of organic sludge carried into the stockyard, and is crushed and mixed. In order to process the organic sludge corresponding to the amount of carry-in every day, the pretreatment within 4 days including the primary storage and the fermentation for 2 weeks in the closed room are performed sequentially for a plurality of closed rooms. is there. 4 days pretreatment is the appropriate time as a pretreatment time for securing the crushing mixing process and moisture adjustment time may be one, two days more periods than the number of days. A closed room fermentation of about two weeks may cause a shift of a few days. In FIG. 1, 56 is a temperature sensor in the sealed chamber, 58 is a soot that guides the moisture in the sludge produced in the crushing and mixing step, the primary storage step, etc., and 60 is a drainage soot.

  Next, the operation of the organic sludge treatment system according to the present embodiment will be described together with the organic sludge treatment method with reference to FIG. The organic sewage sludge RM1, the cow dung RM2, the organic food industrial sludge RM3, and the food residue RM4 are carried into the stock yard 24 of the treatment facility 20 in FIG. 1 (S1). The type of organic sludge that is brought in every day is indefinite, and it is difficult to specify the composition of the type of sludge that is brought into the stockyard every day. For example, there is only one type in the above sludge, and all four types may be mixed. There may be only two types or only three types. For example, the organic sewage sludge RM1 has a water content of about 80%, the cow dung RM2 is about 55%, the organic food industrial sludge RM3 is about 83%, and the food residue RM4 is about 24%. The water content is 80 to 90%. In each sludge, metals, plastic pieces and other non-organic substances are removed in advance by filtering or the like, and only 30 tons of organic substances are carried into the stockyard.

  The organic sludge to be treated carried into the stockyard is transported to the adjacent crushing and mixing unit 12 by, for example, a tire excavator, and is introduced into the mixing and crushing machine installed there together with the microbial powder and mixed and stirred (S2). ). At this time, for example, microbial powder is added to the sludge 10 at a weight ratio of about 1:10 and mixed and stirred.

  After mixing and stirring, for example, particulate sludge having a particle diameter of about 5 mm is formed, and this is further transferred to the primary storage unit 14 at the opposite position across the transfer lane 22 by a transfer means such as a tire shovel. In the primary storage unit, for example, the reversing device reciprocates within the tank of the primary storage unit at a rate of about several times per hour (S3), preventing corruption due to oxygen supply to the organic sludge charged therein and fermentation. We perform curing to prepare easy-to-use conditions. Thus, the pretreatment process is performed. The pretreatment process including the crushing and mixing and the primary storage process is performed, for example, for 4 days.

  Next, about 80 tons of sludge is accumulated in the primary storage unit 14, and on the fifth day, 80 tons of sludge is put into a sealed chamber of the fermentation processing unit 16 having a capacity of, for example, 85 tons at a time. And this process is sequentially performed about each sealed chamber 181-188. Simultaneously with the introduction of the sludge into each sealed chamber, the heated air injection driving device 49 is driven to inject the heated air of about 25 ° C. to 35 ° C. into the treatment target sludge. After the injection, the organic sludge undergoes aerobic fermentation by primary fermentation (S4) about 7 days later, and the sludge temperature rises to about 65 ° C. Furthermore, secondary fermentation (S5) is produced in about the seventh day thereafter, and the temperature in the sludge reaches about 80 to 85 ° C. During this time, warm air of about the above-mentioned normal temperature is blown out from the heated air inlet tube 32, and further, air containing steam from fermentation is sucked from the remaining air portion 42 in the sealed chamber through the suction discharge portion 34 and the deodorizing portion 36. On the other hand, the suction air is deodorized and exhausted to the outside. The suction fan 52 of the suction / discharge section 34 is controlled via a control device so as to operate in conjunction with the temperature detected by the sensor 56 in the residual air section 42, and always maintains the optimum set fermentation conditions. Yes.

Each sealed chamber has a volume that is at least twice as large as the amount of organic sludge carried in, and includes a pretreatment within 4 days including crushing mixing and primary storage, and a closed chamber fermentation for about 2 weeks. By performing sequentially and continuously on the sealed chamber, the organic sludge corresponding to the daily carry-in amount can be treated every day. In addition, by starting the injection of warm air into the organic sludge and performing this sequentially and continuously for all sealed chambers, a fertilizer raw material equivalent to at least the same amount as the treatment input is produced within 24 hours. (S6). When the sludge fermentation is completed, the volume of composted sludge is reduced to about 1/3 of 20t. Then, all the composted sludge after completion is discharged from the first sealed chamber 181, transported to the working space of the bagging processing section 26 and packed in a bag (S 7), and a product can be shipped (S 8). . At this time, for example, the moisture content is adjusted to about 20% to 30%.

FIG. 5 is a table of these process steps, and the first to eighth chambers are each subjected to 4 days of pretreatment and 14 days of fermentation treatment to process a total of 80 tons of sludge. In the figure, after pretreatment for 4 days, 80 tons of sludge is filled in the sealed chambers 181 to 188, and simultaneously, the heating air 32 injection driving is started, and then the fermentation is completed in about 2 weeks to obtain compost. The first room is fermented from the 5th to the 18th, the second room is the 9th to the 22nd, the third room is the 13th to the 26th, and so on. Rotation is repeated and all 8 rooms are used, while 20 tons of sludge is processed daily. In addition, 10 tons of composted products made into bag products at intervals of about 3 days will be completed in the work space.

Hereinafter, by repeating this step by step, it is possible to process a large amount of sludge with a very simple facility that simply creates a sealed space adjacent to the site. That is, 20t of sludge is introduced every day, and about 20t of sludge compost is processed and produced every day after volume reduction after fermentation treatment. That is, the organic sludge fermentation process corresponding to at least the same amount as the process input amount is performed within 24 hours by sequential work. The composted sludge after treatment becomes a target for trading as a valuable resource and brings profits. In the above-described embodiment, eight sealed chambers and eight sealed chamber devices including the sealed chamber are provided, but a larger number may be installed. Moreover, it is good also as a structure which is not only limited to four opposing arrangements of sealed chambers but simply arranged in series.

FIG. 6 shows an example of an analysis result of compost produced by the above processing system and method.

The organic sludge treatment method of the present embodiment includes a step of mixing the powder on which microorganisms are implanted while crushing the organic sludge, a step of storing the organic sludge after mixing and supplying air by a reversing operation, The process of injecting organic sludge supplied with air into the sealed room and allowing it to stand still and blowing heated air continuously from the bottom of the room and injecting it into the organic sludge; Including a step of transpiration to a part, a step of sucking and ventilating a gas in a sealed chamber together with transpiration to a room air portion, and a step of deodorizing the sucked gas. Depending on the work, an organic sludge fermentation treatment equivalent to at least the same amount as the input amount of treatment is performed within 24 hours.

  At this time, the temperature of the heated air into the organic sludge in the sealed room is 25 to 35 degrees, and the microbial fermentation promotes the fermentation after the primary fermentation step in which the internal temperature of the organic sludge rises to about 60 ° C. And a secondary fermentation step of about 85 ° C.

The organic sludge treatment facility of the present invention described above is not limited to the above-described embodiment, and any modification may be made without departing from the essence of the present invention described in the claims. Good.

The treatment facility for organic sludge according to the present invention is a simple facility that treats organic waste discharged from sewage sludge, domestic waste, livestock manure, food residues, food production factories, general offices, and other organic waste. It can handle large volumes effectively.

BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an explanatory plan view of the entire configuration of an organic sludge treatment facility according to an embodiment of the present invention. FIG. 2 is a partially omitted enlarged plan explanatory view of a sealed chamber in the processing facility of FIG. 1. It is an expansion longitudinal cross-section explanatory drawing of the processing facility of the processing facility of the organic sludge of FIG. It is a flowchart figure which shows the processing method by the processing facility of FIG. It is a figure which shows the table | surface of the processing process by the processing facility of FIG. It is a figure of the component table | surface of the compost manufactured by the processing facility of FIG.

12 Crushing and mixing unit 14 Primary storage unit
DESCRIPTION OF SYMBOLS 16 Fermentation process part 18 Sealed chamber apparatus 32 Heated air injection pipe 34 Suction discharge part 36 Deodorizing part Cm1 1st sealed room group, Cm2 2nd sealed room group 181-190 Sealed room

Claims (2)

A crushing and mixing unit that mixes a powder in which microorganisms have been implanted at a predetermined ratio with respect to the organic sludge to be carried, and crushes to a required particle size ;
A primary storage unit that stores and cures the sludge after the crushing and mixing process ,
A fermentation treatment unit for fermenting organic sludge while containing organic sludge after treatment in the primary storage unit and supplying air;
The fermentation processing unit includes a plurality of sealed chamber devices attached thereto,
The sealed chamber apparatus includes a sealed chamber into which organic sludge is charged and left stationary;
A heated air injection pipe for injecting heated air into the organic sludge thrown into the sealed chamber;
A suction discharge unit for sucking and discharging air containing steam generated by microbial fermentation of organic sludge;
A deodorizing part for deodorizing the sucked gas,
In one site, the crushing and mixing unit and the primary storage unit are arranged at opposite positions with the central conveyance space in the middle as a pretreatment unit, and a plurality of sealed processing chambers of the fermentation processing unit and the crushing and mixing unit and primary storage Arranged adjacent to each other, and arranged at the opposite position with the central conveyance space in the middle,
An organic sludge treatment facility characterized in that eight or more sealed chambers are arranged with a volume at least twice the daily amount of organic sludge carried in. The treatment facility for organic sludge according to claim 1, wherein the temperature of the heated air into the organic sludge charged into the sealed chamber is 25 to 35 degrees.

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