JP2005074275A - Thermally stratified spiral flow type fermentor - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a fermentor that is capable of efficiently fermenting organic wastes included in an organic solution to be treated L in a low cost. <P>SOLUTION: The fermentor is provided with a tank body 1, an original solution feeding part 2 to feed the organic solution to be treated L to the bottom part, a first heating device 3 that heats the organic solution to be treated which is sent to the tank body 1 to a fermentation temperature of the intermediate temperature, a second heating device 4 that heats the upper side of the organic solution to be treated L arranged at the middle height within the tank body 1 to a fermentation temperature of the high temperature, a digested solution discharge part 5 which is opened under the liquid surface of the organic solution to be treated L within the tank main body 1, a bio-gas discharge part 6 that is extended from the upper part of the tank body 1, a first heat reserving device 7 that is fitted to the lower side than the second heating device 4 and a second heat preserving device 8 that is fitted to the upper side of the same to outer periphery of the tank body 1. Thus, the fermentor creates the thermally stratified state in the tank body 1 comprised of the lower part intermediate temperature fermentation area 10A where is kept in an almost uniform fermentation temperature atmosphere of the intermediate temperature and the upper part high temperature fermentation area 10B kept in an almost uniform fermentation temperature atmosphere of the high temperature, on the border of the second heating device 4. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

  The present invention relates to a fermenter for decomposing organic waste in an organic treatment liquid by methane bacteria in resource recycling technology such as organic waste, biogas production technology, and microbial reaction technology. is there.

Biogas produced by methane fermentation of organic processing liquids containing organic waste such as household garbage, livestock manure, agricultural residue and sludge in the fermenter (mainly Methane CH ₄ ) can be converted into electric power by a fuel cell, a gas engine generator, a gas turbine generator, or the like, or converted into thermal energy by combustion. Such fermenting technology is extremely important for supplying clean energy and recycling resources.

When producing biogas from the organic treatment liquid as described above, in order to efficiently generate biogas, the organic treatment liquid is subjected to medium temperature fermentation (fermentation in a temperature environment around 35 degrees Celsius). After that, it is effective to perform high temperature fermentation (fermentation in a temperature environment around 55 degrees Celsius). This is to decompose organic treated liquid using methane bacteria (medium temperature methane bacteria and high temperature methane bacteria) active in each temperature environment. For example, when the concentration of organic matter is high, Although fermentation may not be performed properly, fermentation efficiency can be increased by placing a high-temperature fermentation process downstream. Conventionally, as such a technique, for example, one described in Patent Document 1 below is known.
JP 2003-24912 (see FIGS. 2 and 3)

  FIG. 4 is an explanatory view schematically showing a conventional biogas generation system for fermenting an organic treatment liquid at high temperature after intermediate temperature fermentation. Reference numeral 101 in FIG. 4 is an intermediate temperature fermenter. In the intermediate temperature fermenter 101, an organic processing liquid L containing organic waste is heated to about 35 degrees Celsius by a heating device 102, and is passed through a pipe 103. Have been supplied. Since the organic processing liquid L stored in the intermediate temperature fermenter 101 is maintained at the above temperature by the temperature maintaining device 104 provided on the side wall, it is fermented by the intermediate temperature methane bacteria, and the biogas G generated thereby is liquid. The air bubbles rise inside as bubbles B and are collected through the pipe 105 opened to the air chamber 101a on the liquid surface and used as a source of electric power and heat energy. And since the organic type to-be-processed liquid L in the intermediate temperature fermenter 101 is gradually pushed up by the new organic-type to-be-processed liquid L sequentially supplied from the piping 103 to the tank lower part, it is a liquid with a long storage time (fermentation time). From the surface side, it is sent to the high-temperature fermenter 108 by the pump 107 through the pipe 106.

  The organic processing liquid L supplied from the intermediate temperature fermenter 101 to the high temperature fermenter 108 through the pipe 106 is heated from about 35 degrees Celsius suitable for fermentation by the medium temperature methane bacteria by the heating device 109 provided in the middle of the pipe 106. Heated to about 55 degrees Celsius, suitable for fermentation with high-temperature methane bacteria. And since the organic type to-be-processed liquid L stored in the high temperature fermenter 108 is heat-retained at the said temperature by the heat retention apparatus 110 provided in the side wall, it ferments with a high temperature methane microbe, and the biogas G generated by this is generated. The liquid floats as bubbles B, is collected through a pipe 111 opened to the air chamber 108a on the liquid level, and is used together with the biogas G from the intermediate temperature fermenter 101 as a power and heat energy source.

  Further, the organic treatment liquid L in the high-temperature fermentation tank 108 is gradually pushed up by the organic treatment liquid L sequentially supplied from the intermediate temperature fermentation tank 101 to the lower part of the tank through the pipe 106, so that the fermentation has sufficiently progressed. The digestive juice L ′ is sequentially discharged by the pump 113 through the pipe 112 and sent to the next process such as liquid fertilization or waste water treatment.

  Some medium temperature fermenters 101 and high temperature fermenters 108 are provided with rotating stirring blades to stir and mix the organic processing liquid L. In this case, the medium temperature fermenter 101 or the high temperature fermenter is used. It is inevitable that a part of the organic processing liquid L supplied to 108 is discharged from the outlet without being sufficiently fermented. On the other hand, since the extrusion type (piston type) as described above is pushed out to the outlet side in the order of the long storage time (fermentation time), this is not the case.

  However, in the above-described conventional technology, two tanks of the intermediate temperature fermenter 101 and the high temperature fermenter 108 are necessary, and piping, a pump, a heat retaining device and the like must be provided in each of the intermediate temperature fermenter 101 and the high temperature fermenter 108. The cost was inevitable and the installation space had to be large.

  The present invention has been made in view of the above-described problems, and the technical problem is that organic waste contained in an organic treatment liquid can be fermented at low cost and efficiently. It is to provide a fermenter.

  As a means for effectively solving the above technical problem, the temperature-stratified swirl type fermenter according to the invention of claim 1 supplies an organic processing liquid to a tank body and a lower end portion in the tank body. An undiluted solution supply unit, a first heating device that heats the organic processing liquid to be fed into the tank body to a medium temperature fermentation temperature, and an intermediate position between the liquid storage heights in the tank body. A second heating device that heats the organic treatment liquid from a medium temperature fermentation temperature to a high temperature fermentation temperature, and a digestion that is above the second heating device and opens below the surface of the organic treatment liquid in the tank body A liquid discharge part and a biogas discharge part opened in the upper air chamber in the tank body, wherein the stock solution supply part is opened in a direction to give a swirl flow to the organic processing liquid in the tank body It is.

  In addition, the organic treatment liquid here is a liquid that is a mixture of one or more organic wastes such as household waste, livestock manure, agricultural residues and sludge. As is well known, it is a temperature environment of approximately 30 to 40 degrees Celsius suitable for fermentation by a mesophilic methane bacterium, and the high temperature fermentation temperature, as is well known, is a fermentation by a high temperature methane bacterium. It is a temperature environment of approximately 50 to 60 degrees Celsius suitable for the above.

  The temperature-stratified swirl type fermenter according to the invention of claim 2 is the configuration according to claim 1, wherein the organic processing liquid below the second heating device is kept at the intermediate temperature fermentation temperature on the side wall of the tank body. And a second heat retaining device that retains the organic processing liquid above the second heating device at a high temperature fermentation temperature.

  The temperature-stratified swirling flow type fermenter according to the invention of claim 3 is the configuration according to claim 1 or 2, wherein the second heating device is a serpentine tube through which the organic processing liquid can pass uniformly from the lower side to the upper side. Or it consists of coiled piping.

  The temperature-stratified swirl type fermenter according to the invention of claim 4 is the structure according to any one of claims 1 to 3, wherein the opening of the digestive juice discharge part is located substantially at the center of turning of the organic processing liquid. To do.

  According to the temperature stratified swirling flow type fermenter according to the invention of claim 1, a temperature stratification state consisting of an intermediate temperature fermentation region and an upper temperature high temperature fermentation region with a second heating device as a boundary in one tank body. Since it creates and performs medium temperature fermentation in the medium temperature fermentation region and high temperature fermentation in the high temperature fermentation region, the structure is simplified and the installation space can be reduced compared to the conventional two-tank type In addition, since the stirring device is not used, the cost can be reduced. In addition, the organic treatment liquid in the tank body is swirled by the discharge flow from the stock solution supply section, and is sequentially sent out through the lower intermediate temperature fermentation region, the second heating device, and the upper high temperature fermentation region, and the residence time Since it is discharged in the long order, sufficient methane fermentation can be performed.

  According to the temperature stratified swirl type fermenter according to the invention of claim 2, the inside of the tank main body is maintained in a substantially uniform medium temperature fermentation temperature environment by the first heat retaining device with the second heating device as a boundary. In order to create a temperature stratification state between the lower intermediate temperature fermentation area and the upper high temperature fermentation area maintained in a substantially uniform high temperature fermentation temperature environment by the second heat retention device, in the intermediate temperature fermentation area and the high temperature fermentation area High temperature fermentation can be performed stably.

  According to the temperature stratified swirl type fermenter according to the invention of claim 3, the second heating device is composed of a serpentine tube or a coiled pipe through which the organic processing liquid can pass uniformly from the lower side to the upper side. Therefore, the organic processing liquid pushed up from the lower intermediate temperature fermentation region to the upper high temperature fermentation region can be efficiently heated from the intermediate temperature fermentation temperature to the high temperature fermentation temperature.

  According to the temperature-stratified swirling flow type fermenter according to the invention of claim 4, the opening of the digestive juice discharge part is provided substantially at the swirling center of the organic treatment liquid, so that a stable swirl flow in the tank main body is provided. Can be maintained.

  Hereinafter, a preferred embodiment of a temperature stratified swirl type fermenter according to the present invention will be described with reference to the drawings. FIG. 1 is a vertical sectional view showing a schematic configuration of a temperature-stratified swirling flow type fermenter according to the present invention, and FIGS. 2 and 3 are explanatory views showing the principle of generation of swirling flow.

  A temperature-stratified swirling flow type fermenter according to the embodiment shown in FIG. 1 includes a tank body 1, a stock solution supply unit 2 for supplying an organic processing liquid L to the lower part of the tank body 1, and a tank body 1. The first organic heating liquid 3 is heated to a medium temperature fermentation temperature, that is, about 35 degrees Celsius, and the upper organic liquid is disposed at an intermediate height of the liquid storage height in the tank body 1. A second heating device 4 for heating the treatment liquid L from a medium temperature fermentation temperature to a high temperature fermentation temperature, that is, about 55 degrees Celsius, and a liquid of the organic processing liquid L in the tank body 1 above the second heating device 4 A digestive juice discharge part 5 opened below the surface and a biogas discharge part 6 extending from the upper part of the tank body 1 to the outside are provided.

  The tank body 1 is composed of a sealed cylindrical metal container, which is fixed on the foundation 11 and has a first heat retaining device 7 positioned below the second heating device 4 on the outer periphery of the side wall, and an upper side thereof. The 2nd heat retention apparatus 8 located in is attached. Moreover, the outer side of the side wall 1a of the tank main body 1 including the 1st heat retention apparatus 7 and the 2nd heat retention apparatus 8 and the top-plate part 1b is coat | covered with the heat insulation layer 12 and exterior material which consist of heat insulation materials.

The stock solution supply unit 2 includes a liquid supply pipe 21 and a pump 22 provided in the middle thereof. The downstream portion of the liquid supply pipe 21 is branched into a plurality of pipelines. The nozzles 21a and 21a at the downstream ends thereof are positioned in the vicinity of the bottom 1c in the tank body 1 at a symmetrical position of 180 degrees in the circumferential direction on the cylindrical side wall 1a of the tank body 1 as shown in FIG. The opening is rotationally symmetric in a direction substantially tangential to the circumference. Accordingly, the tangential discharge flows F ₁ and F ₁ of the organic processing liquid L discharged from the nozzles 21 a and 21 a of the liquid supply pipe 21 become a circumferential flow along the inner surface of the tank body 1, A uniform swirling flow F ₂ is generated in the entire stored organic processing liquid L.

  As shown in FIG. 3, the nozzles 21a at the downstream end of the liquid supply pipe 21 in the stock solution supply unit 2 are connected to each other in the tangential direction in three or more circumferential directions on the cylindrical side wall 1a of the tank body 1. You may open in rotational symmetry.

  The first heating device 3 is a heat exchanger having a serpentine tube or a coiled pipe 3a through which hot water passes, and is connected to the middle of the liquid supply pipe 21 in the stock solution supply unit 2, and as described above, the tank body 1 The organic processing liquid L sent to the inside is heated to 30 to 40 degrees Celsius, preferably about 35 degrees Celsius.

  The second heating device 4 is a heat exchanger in which serpentine tubes or coiled pipes through which hot water passes are arranged in a plane, and the liquid storage part in the tank body 1 is divided into a lower intermediate temperature fermentation region 10A and an upper high temperature fermentation region 10B. It is provided so that it may be divided. In the second heating device 4, a gap 4 a that allows passage of the organic treatment liquid L and the biogas generated in the lower intermediate temperature fermentation region 10 </ b> A is formed between the serpentine tube or the coiled pipe constituting the second heating device 4. The organic processing liquid L passing through the gap 4a from the lower intermediate temperature fermentation region 10A to the upper high temperature fermentation region 10B is efficiently heated to 50 to 60 degrees Celsius, preferably about 55 degrees Celsius.

The digestive juice discharge unit 5 includes a pipe 51 disposed through the tank body 1 and the heat insulating layer 12 outside the tank body 1, and a pump 52 provided in the middle of the pipe 51 outside the tank body 1. . Inner end opening 51a of the pipe 51 is approximately the central position of the swirling flow F ₂ organic liquid to be treated L in the tank body 1 (revolution center O), substantially axial position of the cylindrical tank body 1 in other words In addition, the liquid of the organic treatment liquid L is not sucked from the upper air chamber 10C near the upper end of the upper high temperature fermentation region 10B, preferably on the liquid surface of the organic treatment liquid L. It is about 15 cm below the surface level h.

  The biogas discharge unit 6 includes a pipe 61 having an opening 61a in the top plate part 1b of the tank body 1 and a pump 62 provided in the middle thereof. The downstream end of the pipe 61 is connected to a gas recovery unit (not shown). It is connected.

  The first heat retaining device 7 is a heat exchanger composed of a coiled pipe or a warm water jacket that is positioned below the installation height of the second heating device 4 and surrounds the outer periphery of the tank body 1. By passing, the organic processing liquid L in the lower intermediate temperature fermentation region 10A of the tank body 1 is kept at about 35 degrees Celsius. Further, the second heat retaining device 8 is a heat exchanger composed of a coiled pipe or a warm water jacket provided so as to surround the outer periphery of the tank body 1 on the upper side of the first heat retaining device 7, and by passing warm water, The temperature of the organic processing liquid L in the upper high temperature fermentation region 10B of the tank body 1 is kept at about 55 degrees Celsius.

  According to the temperature stratified swirling flow type fermenter having the above configuration, the lower intermediate temperature fermentation region 10A for performing intermediate temperature fermentation and the upper high temperature fermentation region 10B for performing high temperature fermentation are provided in a single tank body 1. Therefore, the equipment such as piping is simplified as compared with the conventional two-tank type, so that the cost can be reduced and the installation space can be reduced.

  Next, the process of the organic processing liquid L by the temperature stratified swirl type fermenter of this form will be described. In addition, the organic processing liquid L supplied to the tank main body 1 from the undiluted | stock solution supply part 2 is the slurry which grind | pulverized the household garbage, the slurry which grind | pulverized the residue of agricultural products, etc. in sewage or tap water etc. It is a mixture of one or more organic wastes such as manure and septic tank sludge. In addition, methane bacteria (medium-temperature methane bacteria and high-temperature methane bacteria) necessary for fermentation are usually present in dung, etc., so if you do not need to start up the plant quickly, you do not need to add it. A methane bacterium is added in advance to the organic processing liquid L introduced into the stock solution supply unit 2.

  First, the organic processing liquid L from the stock solution supply unit 2 is heated to about 35 degrees Celsius by the first heating device 3 in the process of being continuously sent to the lower end of the lower intermediate temperature fermentation region 10A in the tank body 1. Is done. On the other hand, in the digestive juice discharge section 5, the pump 52 is driven to discharge the fermented organic processing liquid L (digested liquid L ′) at the same flow rate as the supply flow rate from the stock solution supply section 2, As a result, the liquid level h of the organic processing liquid L stored in the tank body 1 is maintained substantially constant.

As shown in FIG. 2, from the nozzles 21 a, 21 a at the downstream end of the liquid supply pipe 21 in the stock solution supply unit 2 to the outer periphery of the lower end portion of the lower intermediate temperature fermentation region 10 </ b> A in the tank body 1 (near the bottom portion 1 c). The organic processing liquid L supplied into the tank body 1 by the discharge flows F ₁ and F ₁ of the organic processing liquid L discharged in the tangential direction is centered on the vertical axis of the tank body 1. A laminar swirl flow F ₂ is given. The organic processing liquid L is continuously supplied from the nozzles 21a and 21a to the outer periphery of the lower part in the tank body 1 at a constant discharge flow rate, so that the organic processing liquid L is sequentially pushed up from the lower part to the upper part as a piston. go.

  The organic processing liquid L supplied to the lower intermediate temperature fermentation region 10A in the tank body 1 is heated to about 35 degrees Celsius suitable for fermentation by intermediate temperature methane bacteria by the first heating device 3, and the temperature thereof is increased. It is maintained by the heat insulating layer 12 and the first heat retaining device 7. Medium-temperature methane bacteria and high-temperature methane bacteria in the organic treatment liquid L live in both medium-temperature and high-temperature environments. In the medium-temperature environment, the medium-temperature methane bacteria proliferate and act actively. For this reason, in the staying process in the lower intermediate temperature fermentation region 10A, decomposition (medium temperature fermentation) is mainly performed by an intermediate temperature methane bacterium, and biogas G mainly containing methane is generated. The generated biogas G becomes fine bubbles B and floats in the liquid from the lower intermediate temperature fermentation region 10A through the gap 4a of the second heating device 4 to the upper high temperature fermentation region 10B. Released to 10C.

  As described above, the organic processing liquid L is pushed up in a piston-like manner in the lower intermediate temperature fermentation region 10A as the intermediate temperature fermentation progresses. The two heating devices 4 are pushed up to the upper high-temperature fermentation region 10B through the gap 4a between the serpentine tubes or coiled pipes. For this reason, as in the case of forcibly stirring by the stirring device, a part of the organic processing liquid L just supplied to the lower intermediate temperature fermentation region 10A is heated together with the organic processing liquid L having a long residence time. Since it does not move to the fermentation region 10B and is pushed up to the upper high-temperature fermentation region 10B in order from the longest residence time in the lower intermediate-temperature fermentation region 10A, sufficient intermediate-temperature fermentation can be performed. In addition, since a stirring device is unnecessary, the cost is reduced.

  When the organic processing liquid L kept at about 35 degrees Celsius suitable for intermediate temperature fermentation in the lower intermediate temperature fermentation region 10A passes through the gap 4a of the second heating device 4 to the upper high temperature fermentation region 10B, the temperature is high. While being heated to about 55 degrees Celsius suitable for fermentation by methane bacteria, the temperature is maintained by the heat insulating layer 12 and the second heat retaining device 8. For this reason, the inside of the tank main body 1 was maintained in the substantially uniform high temperature fermentation temperature environment and the lower intermediate temperature fermentation region 10A maintained in a substantially uniform medium temperature fermentation temperature environment with the second heating device 4 as a boundary. It is in the temperature stratification state clearly divided into the upper high-temperature fermentation region 10B.

  The high-temperature methane bacterium in the organic treatment liquid L actively propagates and operates in a high-temperature environment. For this reason, the organic treatment liquid L undergoes high-speed decomposition (high-temperature fermentation) mainly with high-temperature methane bacteria during the staying process in the upper high-temperature fermentation region 10B, and generates biogas G mainly composed of methane. . The generated biogas G becomes fine bubbles B, floats in the liquid in the upper high-temperature fermentation region 10B, and is discharged from the liquid surface to the upper air chamber 10C.

Further, the turning force provided by the nozzles 21a and 21a at the downstream end of the liquid supply pipe 21 in the lower intermediate temperature fermentation region 10A is transmitted into the upper high temperature fermentation region 10B through the gap 4a of the second heating device 4. Is done. Moreover, since the discharge port (opening 51a) by the digestive fluid discharge part 5 is located in the turning center O shown in FIG. 2, the organic processing liquid L pushed up to the vicinity of the liquid surface gradually turns while turning. Will move in the centripetal direction. Therefore, without swirling flow F ₂ in the upper hot fermentation region 10B is disturbed, stable turning state is maintained.

Organic liquid to be treated L of the upper hot fermentation region 10B while gradually mixed by swirling flow F _2, to go to the piston to be sequentially pushed up with the progress of high temperature fermentation above, forcibly agitated by the stirring device As in the case where a part of the organic treatment liquid L just sent from the lower intermediate temperature fermentation region 10A to the upper high temperature fermentation region 10B is part of the organic treatment liquid L having a long residence time in the upper high temperature fermentation region 10B. At the same time, it is not discharged from the digestive juice discharge section 5, and sufficient decomposition by high temperature fermentation can be performed. In addition, since a stirring device is unnecessary, the cost is reduced.

  The biogas G generated by the medium temperature fermentation in the lower intermediate temperature fermentation region 10A and the biogas G generated by the high temperature fermentation in the upper high temperature fermentation region 10B are released into the upper air chamber 10C, and the top plate portion 1b of the tank body 1 is obtained. After being collected through the biogas discharge section 6 opened in the opening 61a and subjected to treatment such as removal of moisture and hydrogen sulfide, it is sent to a fuel cell, gas engine generator, gas turbine generator, etc. (not shown) By converting it into electric power, it can also be used as driving energy for the pump 22 in the stock solution supply unit 2, the pump 52 in the digestive fluid discharge unit 5, the pump 62 in the biogas discharge unit 6, and the like. Further, the heat generated by the generator or the like can be used as a heat source for hot water supplied to the first heating device 3, the second heating device 4, the first heat retaining device 7 and the second heat retaining device 8.

  On the other hand, the digested liquid L ′ discharged from the digested liquid discharging unit 5, that is, the liquid to be treated after most of the organic matter is decomposed into methane or the like by sufficient fermentation, is sprayed on pasture and the like by liquid fertilization. Or can be discharged after a predetermined water treatment.

  In addition, the supply flow rate of the organic processing liquid L by the stock solution supply unit 2 is appropriately set in consideration of the residence time (retention days) in the tank body 1 necessary for sufficient fermentation. Moreover, when the swirl speed of the organic processing liquid L in the upper high-temperature fermentation region 10B in the tank body 1 is fast, as shown by a one-dot chain line in FIG. Or it becomes easy to gather the bubble B of the biogas generated in the liquid toward the turning center. Therefore, the biogas G is sucked out from the digestive juice discharge section 5 due to such a phenomenon, and the recovery amount of the biogas G by the biogas discharge section 6 is not reduced from each nozzle 21a, 21a. The discharge speed of the organic processing liquid L is appropriately set.

The present invention is not limited to the embodiment described above. For example, the tank body 1 does not necessarily have a cylindrical shape, and the horizontal cross-sectional shape is substantially as long as a substantially uniform swirl flow F ₂ can be formed by the discharge flow F ₁ from the nozzle 21 a of the stock solution supply unit 2. It may be a square or a substantially regular polygon. The first heating device 3, the second heating device 4, the first heat retaining device 7, and the second heat retaining device 8 can also use an electric heater, and the electric power in this case is generated by using the generated biogas as a fuel cell. Or a gas engine generator or a gas turbine generator.

It is a vertical sectional view showing a schematic structure of a temperature stratified swirl type fermenter according to the present invention. It is explanatory drawing which shows the generation | occurrence | production principle of the swirl flow in a tank by this invention. It is explanatory drawing which shows the generation | occurrence | production principle of the swirl | vortex flow in a tank by this invention. It is explanatory drawing which shows schematically the biogas production | generation system by a prior art.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Tank main body 1a Upper air chamber 2 Raw liquid supply part 21 Liquid supply piping 21a, 21a Nozzle 3 1st heating apparatus 4 2nd heating apparatus 5 Digestive liquid discharge part 6 Biogas discharge part 7 1st heat retention apparatus 8 2nd heat retention apparatus 10A Lower intermediate temperature fermentation area 10B Upper high temperature fermentation area 10C Upper air chamber G Biogas L Organic treatment liquid L 'Digested liquid O Center of rotation

Claims (4)

  A tank main body, a stock solution supply section for supplying an organic processing liquid to the lower end of the tank main body, a first heating device for heating the organic processing liquid sent into the tank main body to a medium temperature fermentation temperature, A second heating device that is disposed at an intermediate position of the liquid storage height in the tank body and heats the organic processing liquid on the upper side thereof from a medium temperature fermentation temperature to a high temperature fermentation temperature, and above the second heating device. A digestive juice discharge part opened below the surface of the organic processing liquid in the tank body, and a biogas discharge part opened in the upper air chamber in the tank body, the stock solution supply part comprising: A temperature-stratified swirl type fermenter characterized by being opened in a direction in which a swirl flow is given to the organic treatment liquid in the body.   On the side wall of the tank body, a first heat retaining device that keeps the organic treatment liquid below the second heating device at a medium temperature fermentation temperature, and an organic treatment liquid above the second heating device at a high temperature fermentation temperature. The temperature-stratified swirl type fermenter according to claim 1, further comprising a second heat retaining device for retaining heat.   The temperature-stratified swirl type fermenter according to claim 1 or 2, wherein the second heating device comprises a serpentine tube or a coiled pipe through which the organic processing liquid can pass uniformly from the lower side to the upper side.   The temperature-stratified swirl type fermenter according to any one of claims 1 to 3, wherein the opening of the digestive juice discharge part is located substantially at the center of swirl of the organic processing liquid.

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