JP6733928B1 - Digestive tank - Google Patents

Digestive tank Download PDF

Info

Publication number
JP6733928B1
JP6733928B1 JP2019223909A JP2019223909A JP6733928B1 JP 6733928 B1 JP6733928 B1 JP 6733928B1 JP 2019223909 A JP2019223909 A JP 2019223909A JP 2019223909 A JP2019223909 A JP 2019223909A JP 6733928 B1 JP6733928 B1 JP 6733928B1
Authority
JP
Japan
Prior art keywords
internal space
digestion tank
vertical direction
digested
space
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
JP2019223909A
Other languages
Japanese (ja)
Other versions
JP2021090926A (en
Inventor
好幸 野呂
好幸 野呂
健介 北田
健介 北田
新川 隆夫
隆夫 新川
間宮 尚
尚 間宮
智樹 栗波
智樹 栗波
行教 長谷川
行教 長谷川
博和 坪井
博和 坪井
好一 加藤
好一 加藤
孝宏 根本
孝宏 根本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kajima Corp
Metawater Co Ltd
Satake Chemical Equipment Mfg Ltd
Original Assignee
Kajima Corp
Metawater Co Ltd
Satake Chemical Equipment Mfg Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kajima Corp, Metawater Co Ltd, Satake Chemical Equipment Mfg Ltd filed Critical Kajima Corp
Priority to JP2019223909A priority Critical patent/JP6733928B1/en
Application granted granted Critical
Publication of JP6733928B1 publication Critical patent/JP6733928B1/en
Publication of JP2021090926A publication Critical patent/JP2021090926A/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Mixers Of The Rotary Stirring Type (AREA)
  • Treatment Of Sludge (AREA)

Abstract

【課題】消化槽の内部空間の全体における被消化物の混合の均一性を向上させることができる消化槽を提供する。【解決手段】被消化物Wを収容する内部空間2を規定しつつ内部空間2の上端部2u及び下端部2bに至るにつれて内部空間2の中心の側に集束する内側面6sを備えた消化槽1Aにおいて、攪拌機構10により内部空間2に収容された被消化物Wが上下方向に平行な軸周りに攪拌され、内部空間2の下端部2bから上方に突出した邪魔板20Aにより、被消化物Wに内部空間2の下端部2bから上方に向う上昇流が形成され、流動不良部が生じ難いため、消化槽1Aの内部空間2の全体における被消化物Wの混合の均一性を向上させることができる。【選択図】図1PROBLEM TO BE SOLVED: To provide a digestion tank capable of improving the uniformity of mixing of digested substances in the entire inner space of the digestion tank. SOLUTION: The digestion tank is provided with an inner side surface 6s that defines an inner space 2 for accommodating a substance to be digested and converges toward the upper end 2u and the lower end 2b of the inner space 2 toward the center side of the inner space 2. In 1A, the digestion target W stored in the internal space 2 is stirred by the stirring mechanism 10 around an axis parallel to the vertical direction, and the digestion target is generated by the baffle plate 20A protruding upward from the lower end portion 2b of the internal space 2. An upward flow is formed in W from the lower end portion 2b of the internal space 2 upward, and a poor flow portion is unlikely to occur. Therefore, to improve the uniformity of mixing of the digested material W in the entire internal space 2 of the digestion tank 1A. You can [Selection diagram] Figure 1

Description

本発明は、消化槽に関するものである。 The present invention relates to a digestion tank.

汚泥等の被消化物を収容しつつ、被消化物を消化するための消化槽が提案されている。例えば、特許文献1には、消化槽の内部の中心部に上下方向に平行にドラフトチューブが設置された消化槽が開示されている。消化槽に収容された被消化物がドラフトチューブの上端から吸い込まれ、ドラフトチューブの下端から吐出される。これにより、消化槽に収容された被消化物が攪拌される。 A digestion tank has been proposed for digesting digestible substances while accommodating digestible substances such as sludge. For example, Patent Document 1 discloses a digestion tank in which a draft tube is installed parallel to the vertical direction in the center of the inside of the digestion tank. The substance to be digested contained in the digestion tank is sucked from the upper end of the draft tube and discharged from the lower end of the draft tube. As a result, the substance to be digested contained in the digestion tank is agitated.

特開平11‐90492号公報Japanese Patent Laid-Open No. 11-90492

ところで、上記技術は被消化物の消化については優れた性能を有するが、ドラフトチューブによる被消化物の攪拌に大きなエネルギーを消費する。そのため、例えば、消化槽の内部に上下方向に平行な回転軸周りに回転するインペラが配置され、インペラが回転することにより、消化槽に収容された被消化物が攪拌される消化槽も提案されている。しかし、この技術では、被消化物の攪拌に必要なエネルギーは低減されるものの、攪拌された被消化物の流速が低い部位も生じ、消化槽の内部空間の全体における被消化物の均一混合については改善の余地がある。 By the way, although the above technique has excellent performance for digesting the digested material, it consumes a large amount of energy for stirring the digested material by the draft tube. Therefore, for example, there is also proposed a digestion tank in which an impeller that rotates around a rotation axis parallel to the vertical direction is arranged inside the digestion tank, and by rotating the impeller, the substance to be digested contained in the digestion tank is stirred. ing. However, with this technology, although the energy required to stir the digested material is reduced, there is also a portion where the flow velocity of the stirred digested material is low, which results in uniform mixing of the digested material in the entire internal space of the digestion tank. There is room for improvement.

そこで本発明は、消化槽の内部空間の全体における被消化物の混合の均一性を向上させることができる消化槽を提供することを目的とする。 Therefore, an object of the present invention is to provide a digestion tank capable of improving the uniformity of mixing of digested substances in the entire internal space of the digestion tank.

本発明は、被消化物を収容する内部空間を規定しつつ内部空間の上端部及び下端部に至るにつれて内部空間の中心の側に集束する内側面を有する側壁と、内部空間に収容された被消化物を上下方向に平行な軸周りに攪拌する攪拌機構と、内部空間の下端部から上方に突出した邪魔板とを備えた消化槽である。 The present invention provides a side wall having an inner side surface that converges toward the center side of the internal space as it reaches the upper end and the lower end of the internal space while defining the internal space that houses the digested material, and the internal space housed in the internal space. The digestion tank is provided with a stirring mechanism for stirring the digested product around an axis parallel to the vertical direction, and a baffle plate protruding upward from the lower end of the internal space.

この構成によれば、被消化物を収容する内部空間を規定しつつ内部空間の上端部及び下端部に至るにつれて内部空間の中心の側に集束する内側面を有する側壁と、内部空間に収容された被消化物を上下方向に平行な軸周りに攪拌する攪拌機構とを備えた消化槽において、攪拌機構により内部空間に収容された被消化物が上下方向に平行な軸周りに攪拌され、内部空間の下端部から上方に突出した邪魔板により、被消化物に内部空間の下端部から上方に向う上昇流が形成され、流動不良部が生じ難いため、消化槽の内部空間の全体における被消化物の混合の均一性を向上させることができる。 According to this configuration, a side wall having an inner side surface that converges toward the center side of the inner space as it reaches the upper end and the lower end of the inner space while defining the inner space that houses the digested material, and is housed in the inner space. In a digestion tank equipped with a stirring mechanism for stirring the digested substance around an axis parallel to the vertical direction, the digestible substance stored in the internal space is stirred around the axis parallel to the vertical direction by the stirring mechanism, The baffle plate that protrudes upward from the lower end of the space forms an upward flow upward from the lower end of the internal space in the digested material, and it is difficult for a poor flow to occur, so digestion in the entire internal space of the digestion tank It is possible to improve the uniformity of mixing of the substances.

また、本発明は、被消化物を収容する内部空間の下端部を規定する内底面を有する底壁と、内部空間を規定し、内底面の周縁部から延在し、内部空間の上端部及び下端部に至るにつれて内部空間の中心の側に集束する内側面を有する側壁と、内部空間に収容された被消化物を上下方向に平行な軸周りに攪拌する攪拌機構と、内底面から上方に突出した邪魔板とを備え、内底面は、内部空間の上端部で側壁の上縁部により規定された上面部よりも広い平坦面を有し、邪魔板は、平坦面から上方に突出している消化槽である。 Also, the present invention defines a bottom wall having an inner bottom surface that defines a lower end portion of the internal space that houses the digested material, defines the internal space, and extends from a peripheral edge portion of the inner bottom surface, and an upper end portion of the internal space and A side wall having an inner side surface that converges toward the center of the inner space as it reaches the lower end, a stirring mechanism that stirs the digested material contained in the inner space around axes parallel to the up-down direction, and upward from the inner bottom surface. And an inner bottom surface having a wider flat surface than the upper surface portion defined by the upper edge portion of the side wall at the upper end portion of the internal space, and the baffle plate protruding upward from the flat surface. It is a digestive tank.

この構成によれば、被消化物を収容する内部空間の下端部を規定する内底面を有する底壁と、内部空間を規定し、内底面の周縁部から延在し、内部空間の上端部及び下端部に至るにつれて内部空間の中心の側に集束する内側面を有する側壁とを備えた消化槽において、攪拌機構により内部空間に収容された被消化物が上下方向に平行な軸周りに攪拌され、内底面から上方に突出した邪魔板により、被消化物に内部空間の下端部から上方に向う上昇流が形成されることに加えて、内底面は、内部空間の上端部で側壁の上縁部により規定された上面部よりも広い平坦面を有し、邪魔板は平坦面から上方に突出しており、より速い上昇流が形成され、流動不良部がより生じ難いため、消化槽の内部空間の全体における被消化物の混合の均一性をさらに向上させることができる。 According to this configuration, the bottom wall having the inner bottom surface that defines the lower end portion of the internal space that houses the digested material, and the inner space that extends from the peripheral edge portion of the inner bottom surface, and the upper end portion of the internal space and In a digestion tank having a side wall having an inner side surface that converges toward the center side of the internal space as it reaches the lower end, the digestion target contained in the internal space is agitated around an axis parallel to the vertical direction by the agitation mechanism. The baffle protruding upward from the inner bottom surface forms an upward flow upward from the lower end of the internal space in the digested material, and the inner bottom surface is the upper edge of the side wall at the upper end of the internal space. Since the baffle plate has a flat surface wider than the upper surface defined by the section, the baffle projects upward from the flat surface, a faster upward flow is formed, and a poor flow part is less likely to occur. It is possible to further improve the uniformity of mixing of the digested material in the whole.

本発明の消化槽では、邪魔板は、平面視で内部空間の下端部の中央部に放射状に配置されていることが好適である。 In the digestive tank of the present invention, it is preferable that the baffle plate is radially arranged at the central portion of the lower end portion of the internal space in a plan view.

この構成によれば、邪魔板は平面視で内部空間の下端部の中央部に放射状に配置されているおり、より速い上昇流が形成され、流動不良部がより生じ難いため、消化槽の内部空間の全体における被消化物の混合の均一性をさらに向上させることができる。 According to this configuration, the baffle plate is radially arranged in the central portion of the lower end portion of the internal space in a plan view, a faster upward flow is formed, and a poor flow portion is less likely to occur. It is possible to further improve the uniformity of the mixture of the digested material in the entire space.

また、攪拌機構は、上下方向に平行なパドルと、パドルを上下方向に平行な軸周りに回転させる回転軸とを有することが好適である。 Further, it is preferable that the stirring mechanism has a paddle that is parallel to the vertical direction and a rotation shaft that rotates the paddle about an axis that is parallel to the vertical direction.

この構成によれば、攪拌機構は、上下方向に平行なパドルと、パドルを上下方向に平行な軸周りに回転させる回転軸とを有し、インペラよりも少ないエネルギーにより被消化物を攪拌することができる。 According to this configuration, the stirring mechanism has a paddle that is parallel to the vertical direction and a rotating shaft that rotates the paddle about an axis that is parallel to the vertical direction, and that stirs the digested material with less energy than the impeller. You can

また、内側面は、上下方向に平行な断面による断面視で曲線を含むことが好適であるが、その限りではない。 Further, it is preferable that the inner side surface includes a curved line in a cross-sectional view taken along a cross section parallel to the vertical direction, but the present invention is not limited thereto.

この構成によれば、内側面は上下方向に平行な断面による断面視で曲線を含むため、死水域が生じ難く、良好な攪拌が行われ、被消化物の質及び温度の均一化、消化ガスのガス分離促進及びスカム発生の防止により有効である。 According to this configuration, since the inner surface includes a curved line in a cross-sectional view that is parallel to the vertical direction, a dead water area is unlikely to occur, good stirring is performed, the quality and temperature of the digested material are made uniform, and the digestion gas is digested. It is effective for promoting gas separation and preventing scum generation.

また、内側面は、上下方向に平行な断面による断面視で、内部空間の上端部と下端部との上下方向の距離とが等しい中間部で、内部空間の上端部及び下端部に至るにつれて内部空間の中心の側に集束する曲線を含むことが好適である。 Further, the inner side surface is a middle part where the vertical distance between the upper end portion and the lower end portion of the internal space is the same in a cross-sectional view taken along a cross section parallel to the vertical direction, and the inner surface becomes the inner portion as it reaches the upper end portion and the lower end portion of the internal space. It is preferred to include a converging curve on the side of the center of the space.

この構成によれば、内側面は、上下方向に平行な断面による断面視で、内部空間の上端部と下端部との上下方向の距離とが等しい中間部で、内部空間の上端部及び下端部に至るにつれて内部空間の中心の側に集束する曲線を含むため、被消化物を収容する内部空間の中間部で死水域が生じ難く、良好な攪拌が行われ、被消化物の質及び温度の均一化、消化ガスのガス分離促進及びスカム発生の防止により有効である。 According to this configuration, the inner side surface is an intermediate portion where the vertical distance between the upper end portion and the lower end portion of the internal space is equal to each other in a cross-sectional view taken along a cross section parallel to the vertical direction. Since it includes a curve that converges toward the center of the internal space as it reaches, the dead water area is unlikely to occur in the middle part of the internal space that houses the digested material, good stirring is performed, and the quality and temperature of the digested material It is effective for homogenization, promotion of gas separation of digestion gas, and prevention of scum generation.

本発明の消化槽によれば、消化槽の内部空間の全体における被消化物の混合の均一性を向上させることができる。 According to the digester tank of the present invention, it is possible to improve the uniformity of mixing of the digested material in the entire inner space of the digester tank.

(A)は第1実施形態に係る消化槽を示す縦断面図であり、(B)は(A)のα線による横断面図である。(A) is a vertical cross-sectional view showing the digestion tank according to the first embodiment, and (B) is a horizontal cross-sectional view taken along the line α of (A). 従来の消化槽の内部空間での被消化物の流動を示す図である。It is a figure which shows the flow of the to-be-digested substance in the internal space of the conventional digestion tank. 従来の消化槽の内部空間での被消化物の流動を示す図である。It is a figure which shows the flow of the to-be-digested substance in the internal space of the conventional digestion tank. 第1実施形態に係る消化槽の内部空間での被消化物の流動を示す図である。It is a figure which shows the flow of the to-be-digested substance in the internal space of the digestion tank which concerns on 1st Embodiment. (A)は第2実施形態に係る消化槽を示す縦断面図であり、(B)は(A)のβ線による横断面図である。(A) is a vertical cross-sectional view showing a digestive tank according to the second embodiment, and (B) is a horizontal cross-sectional view taken along the β line of (A). 第2実施形態に係る消化槽の内部空間での被消化物の流動を示す図である。It is a figure which shows the flow of the to-be-digested substance in the internal space of the digestion tank which concerns on 2nd Embodiment. 実験例におけるパドル又はインペラの動力に対する内部空間の被消化物の平均流速を示すグラフである。It is a graph which shows the average flow velocity of the to-be-digested substance of the internal space with respect to the power of a paddle or an impeller in an experiment example. 実験例におけるパドルの先端の周速度に対する内部空間の被消化物の循環量を示すグラフである。It is a graph which shows the circulation amount of the digested material in the internal space with respect to the peripheral velocity of the tip of the paddle in the experimental example. 実験例における攪拌機構の動力に対する内部空間の被消化物の循環量を示すグラフである。It is a graph which shows the circulation amount of the digested material in the internal space with respect to the power of the stirring mechanism in the experimental example.

以下、図面を参照しつつ本発明に係る消化槽について詳細に説明する。図1(A)及び図1(B)に示すように、本発明の第1実施形態に係る消化槽1Aは、汚泥等の被消化物Wを収容する内部空間2と内部空間2を覆う外殻3とから構成されている。消化槽1Aは、全体として卵形の形状を有する。消化槽1Aは、その下部に台座部4を備える。消化槽1Aが安定して設置されるために、台座部4は地中Eに埋設され、不図示の底版の上に載置されている。消化槽1Aは、例えば、全高が20〜30mであり、全幅が10〜20mであり、容量が2000〜4000mである。 Hereinafter, the digestion tank according to the present invention will be described in detail with reference to the drawings. As shown in FIG. 1(A) and FIG. 1(B), the digestion tank 1A according to the first embodiment of the present invention has an internal space 2 for accommodating an object to be digested W such as sludge and an external space for covering the internal space 2. It is composed of a shell 3. The digestive tank 1A has an oval shape as a whole. 1 A of digestive tanks are equipped with the pedestal part 4 in the lower part. In order for the digestion tank 1A to be stably installed, the pedestal portion 4 is embedded in the ground E and placed on a bottom plate (not shown). The digestion tank 1A has, for example, a total height of 20 to 30 m, a total width of 10 to 20 m, and a capacity of 2000 to 4000 m 3 .

消化槽1Aは、被消化物Wを収容する内部空間2の下端部2bを規定する内底面5bを有する底壁5Aを備える。消化槽1Aは、内部空間2を規定しつつ、内底面5bの周縁部5pから内部空間2の外側に向って斜め上方に延在し、内部空間2の上端部2u及び下端部2bに至るにつれて内部空間2の中心の側に集束する内側面6sを有する側壁6を備える。本実施形態では、内底面5bは、内部空間2の上端部2uで側壁6の上縁部6uにより規定された上面部7よりも狭い。内底面5bの直径は、例えば、0.5〜1.5mである。なお、本実施形態では、内底面5bは省略され、内側面6sのみで内部空間2が規定されてもよい。内側面6sは、上下方向に平行な断面による断面視で、下部と上部との間に曲線6cを含む。より詳細には、内側面6sは、上下方向に平行な断面による断面視で、内部空間2の上端部2uと下端部2bとの上下方向の距離とが等しい中間部2mで、内部空間2の上端部2u及び下端部2bに至るにつれて内部空間2の中心の側に集束する曲線6Cを含む。内側面6sは、上下方向に平行な断面による断面視で、曲線6c,6Cを除いた下部及び上部に直線を含む。 The digestion tank 1A includes a bottom wall 5A having an inner bottom surface 5b that defines a lower end portion 2b of the internal space 2 that stores the digested material W. The digestion tank 1A extends obliquely upward from the peripheral edge portion 5p of the inner bottom surface 5b toward the outside of the inner space 2 while defining the inner space 2, and reaches the upper end portion 2u and the lower end portion 2b of the inner space 2. A side wall 6 having an inner side surface 6s that focuses on the center side of the internal space 2 is provided. In the present embodiment, the inner bottom surface 5b is narrower than the upper surface portion 7 defined by the upper edge portion 6u of the side wall 6 at the upper end portion 2u of the internal space 2. The diameter of the inner bottom surface 5b is, for example, 0.5 to 1.5 m. In the present embodiment, the inner bottom surface 5b may be omitted and the inner space 2 may be defined only by the inner side surface 6s. The inner surface 6s includes a curve 6c between the lower portion and the upper portion in a cross-sectional view taken along a cross section parallel to the vertical direction. More specifically, the inner side surface 6s is an intermediate portion 2m in which the vertical distance between the upper end portion 2u and the lower end portion 2b of the internal space 2 is the same in a cross-sectional view taken along a cross section parallel to the vertical direction. It includes a curve 6C that converges toward the center of the internal space 2 as it reaches the upper end 2u and the lower end 2b. The inner side surface 6s includes straight lines in the lower and upper portions excluding the curves 6c and 6C in a cross-sectional view taken along a cross section parallel to the vertical direction.

本実施形態の消化槽1Aでは、内部空間2の全高に対する全幅の比率は、例えば、0.62〜0.72である。また、内部空間2の全幅に対する内底面5bの直径の比率は、例えば、0.03〜0.09である。内部空間2の全幅に対する上面部7の直径の比率は、例えば、0.12〜0.36である。内部空間2の全幅に対する内側面6sの中間部2mの曲線6Cの曲率半径の比率は、例えば、0.62〜0.74である。内側面6sの中間部2mの曲線6Cは、例えば、90°程度の円弧である。上下方向に平行な断面による断面視で、内側面6sの曲線6c及び内側面6sの中間部2mの曲線6Cを除いた下部及び上部の直線の水平からの角度は、例えば、40°〜50°である。 In the digestion tank 1A of this embodiment, the ratio of the total width to the total height of the internal space 2 is, for example, 0.62 to 0.72. The ratio of the diameter of the inner bottom surface 5b to the total width of the internal space 2 is, for example, 0.03 to 0.09. The ratio of the diameter of the upper surface portion 7 to the entire width of the internal space 2 is, for example, 0.12 to 0.36. The ratio of the curvature radius of the curve 6C of the intermediate portion 2m of the inner side surface 6s to the total width of the inner space 2 is, for example, 0.62 to 0.74. The curve 6C of the middle portion 2m of the inner surface 6s is, for example, an arc of about 90°. In a cross-sectional view taken along a plane parallel to the vertical direction, the angle from the horizontal of the lower and upper straight lines excluding the curve 6c of the inner side surface 6s and the curve 6C of the middle portion 2m of the inner side surface 6s is, for example, 40° to 50°. Is.

消化槽1Aは、内部空間2に収容された被消化物Wを上下方向に平行な軸周りに攪拌する攪拌機構10を備える。攪拌機構10は、上下方向に平行なパドル11と、パドル11を上下方向に平行な軸周りに回転させる回転軸12と、回転軸12を回転させる動力源である駆動部13を有する。駆動部13は上面部7に配置された電動機である。駆動部13から、上下方向に平行な回転軸12を介してパドル11が吊下げられている。なお、上下方向に平行な軸周りとは、例えば、攪拌の軸がほぼ垂直であることを意味する。また、上下方向に平行なパドル11とは、例えば、パドルがほぼ垂直であることを意味する。また、パドル11を上下方向に平行な軸周りに回転させる回転軸12とは、例えば、回転軸12がほぼ垂直であることを意味する。パドル11の上端部の高さにおける内部空間2の直径である槽径Dhに対して、パドルの直径である翼径dは、翼径d/槽径Dh=0.1〜0.95の範囲が好ましく、翼径d/槽径Dh=0.25〜0.8の範囲がより好ましい。 1 A of digestive tanks are equipped with the stirring mechanism 10 which stirs the to-be-digested object W accommodated in the internal space 2 around the axis|shaft parallel to an up-down direction. The stirring mechanism 10 includes a paddle 11 that is parallel to the vertical direction, a rotating shaft 12 that rotates the paddle 11 around an axis that is parallel to the vertical direction, and a drive unit 13 that is a power source that rotates the rotating shaft 12. The drive unit 13 is an electric motor arranged on the upper surface portion 7. A paddle 11 is suspended from a drive unit 13 via a rotary shaft 12 parallel to the vertical direction. The term “around an axis parallel to the vertical direction” means that the axis of stirring is substantially vertical, for example. Further, the paddle 11 which is parallel to the vertical direction means that the paddle is substantially vertical, for example. Further, the rotating shaft 12 that rotates the paddle 11 around an axis parallel to the vertical direction means that the rotating shaft 12 is substantially vertical, for example. With respect to the tank diameter Dh which is the diameter of the internal space 2 at the height of the upper end of the paddle 11, the blade diameter d which is the diameter of the paddle is in the range of blade diameter d/tank diameter Dh=0.1 to 0.95. Is preferable, and the range of blade diameter d/tank diameter Dh=0.25 to 0.8 is more preferable.

図1(A)及び図1(B)に示すように、消化槽1Aは、内部空間2の下端部2bから上方に突出した邪魔板20Aを備える。本実施形態では、邪魔板20Aは、内底面5b及び内側面6sの下部から上方に突出している。図1(B)に示すように、邪魔板20Aは、平面視で内部空間2の下端部2bの中央部2cに放射状に配置されている。本実施形態では、4枚程度の邪魔板20Aが内底面5bの中心5cを囲繞するように互いに間隔を空けつつ、十字状をなすように放射状に配置されている。内部空間2の槽径Dhに対して、邪魔板20Aが内底面5b及び内側面6sの下部から上方に突出している範囲の直径である邪魔板径dRADは、邪魔板径dRAD/槽径Dh=0.05〜1.0の範囲が好ましく、邪魔板径dRAD/槽径Dh=0.25〜0.8の範囲がより好ましい。パドル11の翼径dに対して、邪魔板20Aの内底面5bからの突出長である邪魔板突出長Lは、邪魔板突出長L/翼径d=0.05〜0.8の範囲が好ましく、邪魔板突出長L/翼径d=0.1〜0.6の範囲がより好ましい。 As shown in FIGS. 1(A) and 1(B), the digestion tank 1A includes a baffle plate 20A protruding upward from a lower end portion 2b of the internal space 2. In the present embodiment, the baffle plate 20A projects upward from the lower portions of the inner bottom surface 5b and the inner side surface 6s. As shown in FIG. 1(B), the baffle plate 20A is radially arranged in the central portion 2c of the lower end portion 2b of the internal space 2 in a plan view. In the present embodiment, about four baffle plates 20A are radially arranged in a cross shape while being spaced from each other so as to surround the center 5c of the inner bottom surface 5b. With respect to the tank diameter Dh of the internal space 2, the baffle plate diameter dRAD, which is the diameter of the range in which the baffle plate 20A projects upward from the lower portions of the inner bottom surface 5b and the inner side surface 6s, is the baffle plate diameter dRAD/tank diameter Dh= The range of 0.05 to 1.0 is preferable, and the range of baffle plate diameter dRAD/tank diameter Dh=0.25 to 0.8 is more preferable. With respect to the blade diameter d of the paddle 11, the baffle plate protrusion length L, which is the protrusion length from the inner bottom surface 5b of the baffle plate 20A, is in the range of baffle plate protrusion length L/blade diameter d=0.05 to 0.8. The range of baffle plate protrusion length L/blade diameter d=0.1 to 0.6 is more preferable.

なお、内部空間2の下端部2bから上方に突出した邪魔板20Aとは、必ずしも邪魔板20Aが内部空間2の下端部2b及び内底面5bに接していることを要しない。例えば、内部空間2の下端部2bから上方に突出した邪魔板20Aとは、邪魔板20Aの下端と内底面5bとの間に、邪魔板20Aの内底面5bからの突出長の1/10〜1/5程度の隙間を有する場合も含まれる。内部空間2の下端部2bから上方に突出した邪魔板20Aとは、内底面5bのみから上方に突出していてもよく、内側面6sの下部のみから上方に突出していてもよい。 The baffle plate 20A protruding upward from the lower end portion 2b of the inner space 2 does not necessarily mean that the baffle plate 20A is in contact with the lower end portion 2b and the inner bottom surface 5b of the inner space 2. For example, the baffle plate 20A projecting upward from the lower end portion 2b of the internal space 2 means that between the lower end of the baffle plate 20A and the inner bottom surface 5b, 1/10 to 10% of the projecting length from the inner bottom surface 5b of the baffle plate 20A. It also includes the case where there is a gap of about 1/5. The baffle plate 20A projecting upward from the lower end portion 2b of the internal space 2 may project upward only from the inner bottom surface 5b, or may project upward only from the lower part of the inner side surface 6s.

また、なお、平面視で内部空間2の下端部2bの中央部2cとは、必ずしも厳密に内部空間2の下端部2bの中心であることを要しない。平面視で内部空間2の下端部2bの中央部2cは、内部空間2の下端部2bの中心であることが望ましいが、その限りではない。 In addition, the center portion 2c of the lower end portion 2b of the internal space 2 does not necessarily have to be exactly the center of the lower end portion 2b of the internal space 2 in plan view. The center portion 2c of the lower end portion 2b of the internal space 2 is preferably the center of the lower end portion 2b of the internal space 2 in a plan view, but is not limited thereto.

また、邪魔板20Aが平面視で内部空間2の下端部2bの中央部2cに放射状に配置されているとは、必ずしも邪魔板20Aが内底面5bの中心5c及び中心5cの上方に存在していることを要しない。例えば、本実施形態のように、複数の邪魔板20Aが内底面5bの中心5cを囲繞するように互いに間隔を空けつつ、内部空間2の外側に延在していてもよい。また、邪魔板20Aが平面視で内部空間2の下端部2bの中央部2cに放射状に配置されているとは、必ずしも邪魔板20Aが内底面5bの中心5cを通る直線及び内底面5bの中心5cを通る直線の上方に存在していることを要しない。例えば、邪魔板20Aが内底面5bの中心5cを通る直線及び内底面5bの中心5cを通る直線の上方から離隔した位置に配置され、内部空間2の外側に延在していてもよい。また、放射状に配置されているとは、邪魔板20Aが平面視で直線ではなく、曲線をなしていてもよい。 Further, the baffle plate 20A being arranged radially in the central portion 2c of the lower end portion 2b of the internal space 2 in the plan view means that the baffle plate 20A is necessarily present above the center 5c of the inner bottom surface 5b and the center 5c. You don't need to be. For example, as in the present embodiment, the plurality of baffles 20A may extend to the outside of the internal space 2 while being spaced apart from each other so as to surround the center 5c of the inner bottom surface 5b. Further, the fact that the baffle plate 20A is radially arranged in the central portion 2c of the lower end portion 2b of the inner space 2 in a plan view means that the baffle plate 20A does not necessarily mean a straight line passing through the center 5c of the inner bottom surface 5b and the center of the inner bottom surface 5b. It does not need to exist above the straight line passing through 5c. For example, the baffle plate 20A may be arranged at a position separated from above a straight line passing through the center 5c of the inner bottom surface 5b and a straight line passing through the center 5c of the inner bottom surface 5b, and may extend outside the inner space 2. Further, the radial arrangement means that the baffle plate 20A may have a curved line in a plan view instead of a straight line.

本実施形態によれば、被消化物Wを収容する内部空間2を規定しつつ内部空間2の上端部2u及び下端部2bに至るにつれて内部空間2の中心の側に集束する内側面6sを備えた消化槽1Aにおいて、攪拌機構10により内部空間2に収容された被消化物Wが上下方向に平行な軸周りに攪拌され、内部空間2の下端部2bから上方に突出した邪魔板20Aにより、被消化物Wに内部空間2の下端部2bから上方に向う上昇流が形成され、流動不良部が生じ難いため、消化槽1Aの内部空間2の全体における被消化物Wの混合の均一性を向上させることができる。 According to this embodiment, the inner side surface 6s that defines the inner space 2 for accommodating the digested substance W and converges toward the center side of the inner space 2 toward the upper end 2u and the lower end 2b of the inner space 2 is provided. In the digestion tank 1A, the digestion target W stored in the internal space 2 is stirred by the stirring mechanism 10 around an axis parallel to the vertical direction, and the baffle plate 20A protruding upward from the lower end portion 2b of the internal space 2 causes An upward flow is formed in the digested material W from the lower end portion 2b of the internal space 2 upward, and a poor flow portion is unlikely to occur. Therefore, the uniformity of the digested material W in the entire internal space 2 of the digestion tank 1A is made uniform. Can be improved.

例えば、図2に示すように、消化槽100では、消化槽100の内部空間2の中心部に上下方向に平行にドラフトチューブ31が設置されている。消化槽100に収容された被消化物Wがドラフトチューブ31の上端から吸い込まれ、ドラフトチューブ31の下端から吐出される。これにより、消化槽100に収容された被消化物Wが攪拌される。なお、以下の図2、図3、図4及び図6において、内部空間2に矢印で示すフローは、実線、破線及び点線の順に流速が低いことを示す。 For example, as shown in FIG. 2, in the digestion tank 100, a draft tube 31 is installed in the center of the internal space 2 of the digestion tank 100 in parallel with the vertical direction. The digested material W stored in the digestion tank 100 is sucked from the upper end of the draft tube 31 and discharged from the lower end of the draft tube 31. As a result, the digested material W stored in the digestion tank 100 is agitated. In FIGS. 2, 3, 4, and 6 below, the flow indicated by the arrow in the internal space 2 indicates that the flow velocity is low in the order of the solid line, the broken line, and the dotted line.

このような消化槽100では、ドラフトチューブ31から内底面5bに強い吐出流が発生するが、内底面5bで大きく減衰されてしまい、全体的に非常に緩い攪拌となる。また、内部空間2に破線の矢印及び点線の矢印で示すように、多くの領域で流速が低くなり、被消化物Wが汚泥である場合に、濃縮汚泥と消化汚泥との混合が十分ではない。また、フローに偏りがあり、内部空間2の下部でショートパスによる局所的な循環流が生じている。 In such a digestion tank 100, a strong discharge flow is generated from the draft tube 31 to the inner bottom surface 5b, but is greatly attenuated at the inner bottom surface 5b, resulting in a very gentle stirring as a whole. In addition, as shown by the broken line arrow and the dotted line arrow in the internal space 2, when the flow velocity is low in many areas and the digested material W is sludge, the mixture of the concentrated sludge and the digested sludge is not sufficient. .. In addition, the flow is biased, and a local circulation flow due to a short path occurs in the lower portion of the internal space 2.

また、図3に示すように、消化槽200では、内部空間2に上下方向に平行な回転軸42の周りに回転するインペラ41が配置され、インペラ41が回転することにより、消化槽100に収容された被消化物Wが攪拌される。このような消化槽200では、内部空間2に実線の矢印で示すように、内部空間2の下部でショートパスしたフローとなり、内部空間2の上部と下部で分割したフローパターンが形成される。 In addition, as shown in FIG. 3, in the digestion tank 200, an impeller 41 that rotates around a rotation axis 42 that is parallel to the vertical direction is arranged in the internal space 2, and the impeller 41 rotates to accommodate the impeller 41 in the digestion tank 100. The digested product W thus prepared is stirred. In such a digestion tank 200, as shown by a solid arrow in the internal space 2, the flow is short-passed in the lower part of the internal space 2, and a flow pattern divided into the upper part and the lower part of the internal space 2 is formed.

また、消化槽200では、内部空間2に点線の矢印で示すように、内部空間2の下端部2bの中央部2cでは、淀み領域が広がるため、汚泥等の被消化物W中の比重の大きい固形物質等が堆積しやすい。また、消化槽200では、内部空間2における下端部2bの中央部2c付近及び内側面6sの近傍で流速の低い領域が見られる。また、消化槽100では、汚泥等の被消化物Wの混合作用が十分ではなく、温度ムラが生じやすく、スカムの発生が懸念される。 Further, in the digestion tank 200, as shown by a dotted arrow in the internal space 2, in the central portion 2c of the lower end portion 2b of the internal space 2, the stagnation region expands, so that the specific gravity in the digested material W such as sludge is large. Solid substances are likely to accumulate. Further, in the digestion tank 200, a region having a low flow velocity can be seen near the central portion 2c of the lower end portion 2b in the internal space 2 and near the inner side surface 6s. Further, in the digestion tank 100, the action of mixing the digested material W such as sludge is not sufficient, temperature unevenness is likely to occur, and scum may be generated.

一方、図4の内部空間2に実線の矢印で示すように、本実施形態の消化槽1Aでは、内部空間2の下端部2bの中央部2cから上昇流が形成され、内部空間2での流動不良部がみられず、良好な流動性が得られる。また、本実施形態の消化槽1Aでは、内部空間2に被消化物Wの大循環流が形成されており、内部空間2の被消化物Wの全体を一様に攪拌することができる。また、本実施形態の消化槽1Aでは、内部空間2のほとんどの領域で、十分な流速を確保でき、堆積やスカム発生の心配が少ない。 On the other hand, in the digestion tank 1A of the present embodiment, an upward flow is formed from the central portion 2c of the lower end portion 2b of the internal space 2 as indicated by the solid arrow in the internal space 2 of FIG. No defective parts are seen and good fluidity is obtained. Further, in the digestion tank 1A of the present embodiment, the large circulation flow of the digested material W is formed in the internal space 2, and the entire digested material W in the internal space 2 can be uniformly stirred. In addition, in the digestion tank 1A of the present embodiment, a sufficient flow velocity can be secured in almost all areas of the internal space 2, and there is little concern about accumulation or scum generation.

また、本実施形態では、邪魔板20Aは平面視で内部空間2の下端部2bの中央部2cに放射状に配置されており、より速い上昇流が形成され、流動不良部がより生じ難いため、消化槽1Aの内部空間2の全体における被消化物Wの混合の均一性をさらに向上させることができる。 Further, in the present embodiment, the baffle plate 20A is radially arranged in the central portion 2c of the lower end portion 2b of the internal space 2 in a plan view, a faster upward flow is formed, and a poor flow portion is less likely to occur. It is possible to further improve the uniformity of mixing of the digested material W in the entire inner space 2 of the digestion tank 1A.

また、本実施形態では、攪拌機構10は、上下方向に平行なパドル11と、パドル11を上下方向に平行な軸周りに回転させる回転軸12とを有し、従来の消化槽100のようなインペラ41よりも少ないエネルギーにより被消化物Wを攪拌することができる。 In addition, in the present embodiment, the stirring mechanism 10 has a paddle 11 that is parallel to the vertical direction and a rotary shaft 12 that rotates the paddle 11 around an axis that is parallel to the vertical direction. The digested material W can be stirred with less energy than the impeller 41.

また、本実施形態では、内側面6sは上下方向に平行な断面による断面視で曲線6cを含むため、死水域が生じ難く、良好な攪拌が行われ、被消化物Wの質及び温度の均一化、消化ガスのガス分離促進及びスカム発生の防止により有効である。 In addition, in the present embodiment, since the inner surface 6s includes the curve 6c in a cross-sectional view in a cross section parallel to the vertical direction, a dead water area is unlikely to occur, good stirring is performed, and the quality and temperature of the digested material W are uniform. It is effective in promoting gasification, promoting gas separation of digestion gas, and preventing scum generation.

また、本実施形態では、内側面6sは、上下方向に平行な断面による断面視で、内部空間2の上端部2uと下端部2bとの上下方向の距離とが等しい中間部2mで、内部空間2の上端部2u及び下端部2bに至るにつれて内部空間2の中心の側に集束する曲線2Cを含むため、被消化物Wを収容する内部空間2の中間部2mで死水域が生じ難く、良好な攪拌が行われ、被消化物の質及び温度の均一化、消化ガスのガス分離促進及びスカム発生の防止により有効である。 Further, in the present embodiment, the inner surface 6s is an intermediate portion 2m in which the vertical distance between the upper end portion 2u and the lower end portion 2b of the internal space 2 is equal to the internal space 2m in a cross-sectional view taken along a cross section parallel to the vertical direction. 2 includes a curved line 2C that converges toward the center side of the internal space 2 as it reaches the upper end 2u and the lower end 2b of the internal space 2, so that a dead water area is unlikely to occur in the intermediate portion 2m of the internal space 2 that stores the digested material W, which is good. It is effective in that the quality and temperature of the digested material are made uniform, the gas separation of the digested gas is promoted, and the generation of scum is prevented.

以下、本発明の第2実施形態について説明する。図5(A)及び図5(B)に示すように、本実施形態では、消化槽1Bは、被消化物Wを収容する内部空間2の下端部2bを規定する内底面5bを有する底壁5Bを備える。本実施形態では、内底面5bは必須の構成である。一方、上記第1実施形態と同様に、側壁6の内側面6sは、内部空間2を規定しつつ、内底面5bの周縁部5pから内部空間2の外側に向って斜め上方に延在し、内部空間2の上端部2u及び下端部2bに至るにつれて内部空間2の中心の側に集束する。内側面6sは、上下方向に平行な断面による断面視で曲線6cを含む。内側面6sは、上下方向に平行な断面による断面視で、内部空間2の上端部2uと下端部2bとの上下方向の距離とが等しい中間部2mで、内部空間2の上端部2u及び下端部2bに至るにつれて内部空間2の中心の側に集束する曲線6Cを含む。内側面6sは、上下方向に平行な断面による断面視で、曲線6cを含む下部を除いた上部に直線を含む。 The second embodiment of the present invention will be described below. As shown in FIG. 5(A) and FIG. 5(B), in the present embodiment, the digestion tank 1B has a bottom wall having an inner bottom surface 5b that defines a lower end portion 2b of the internal space 2 that stores the digested material W. With 5B. In this embodiment, the inner bottom surface 5b is an essential component. On the other hand, similarly to the first embodiment, the inner side surface 6s of the side wall 6 defines the inner space 2 and extends obliquely upward from the peripheral portion 5p of the inner bottom surface 5b toward the outer side of the inner space 2, As it reaches the upper end 2u and the lower end 2b of the internal space 2, the light is focused toward the center of the internal space 2. The inner side surface 6s includes a curve 6c in a cross-sectional view taken along a cross section parallel to the vertical direction. The inner side surface 6s is a middle portion 2m in which the vertical distance between the upper end portion 2u and the lower end portion 2b of the internal space 2 is equal to the upper end portion 2u and the lower end portion of the internal space 2 in a cross-sectional view in a cross section parallel to the vertical direction. It includes a curve 6C that converges toward the center of the internal space 2 as it reaches the portion 2b. The inner side surface 6s includes a straight line in the upper part except the lower part including the curve 6c in a cross-sectional view taken along a cross section parallel to the vertical direction.

内底面5bは、内部空間2の上端部2uで側壁6の上縁部6uにより規定された上面部7よりも広い平坦面5sを有する。平坦面5sを有するとは、例えば、平坦面5sの直径に対して3%以下の起伏及び傾斜のいずれかを平坦面5sが有している場合を含む。本実施形態では、平坦面5sは水平方向に対してほぼ平行な平面である。本実施形態では、内底面5bは全て平坦面5sである。内底面5bは、例えば、上面部7の2〜4倍の直径を有する。内底面5bの直径は、例えば、5〜15mである。消化槽1Bの全高、全幅及び容量については、上記第1実施形態の消化槽1Aと同様である。また、攪拌機構10についても、上記第1実施形態の消化槽1Aと同様である。また、翼径d/槽径Dhの好ましい範囲についても、上記第1実施形態の消化槽1Aと同様である。 The inner bottom surface 5b has a flat surface 5s wider than the upper surface portion 7 defined by the upper edge portion 6u of the side wall 6 at the upper end portion 2u of the internal space 2. Having the flat surface 5s includes, for example, a case where the flat surface 5s has any of undulations and inclinations of 3% or less with respect to the diameter of the flat surface 5s. In the present embodiment, the flat surface 5s is a plane substantially parallel to the horizontal direction. In this embodiment, the inner bottom surface 5b is a flat surface 5s. The inner bottom surface 5b has a diameter that is, for example, 2 to 4 times that of the upper surface portion 7. The diameter of the inner bottom surface 5b is, for example, 5 to 15 m. The total height, width and capacity of the digestion tank 1B are the same as those of the digestion tank 1A of the first embodiment. The stirring mechanism 10 is also the same as that of the digestion tank 1A of the first embodiment. The preferable range of blade diameter d/tank diameter Dh is also the same as in the digestion tank 1A of the first embodiment.

本実施形態の消化槽1Bでは、内部空間2の全高に対する全幅の比率は、例えば、0.82〜0.92である。また、内部空間2の全幅に対する内底面5bの直径の比率は、例えば、0.54〜0.64である。内部空間2の全幅に対する上面部7の直径の比率は、例えば、0.12〜0.36である。内部空間2の全幅に対する内側面6sの曲線6c,6Cの曲率半径の比率は、例えば、0.62〜0.74である。内側面6sの中間部2mの曲線6Cは、例えば、90°程度の円弧である。上下方向に平行な断面による断面視で、内側面6sの曲線6c及び内側面6sの中間部2mの曲線6Cを除いた上部の直線の水平からの角度は、例えば、40°〜50°である。 In the digestion tank 1B of this embodiment, the ratio of the total width to the total height of the internal space 2 is, for example, 0.82 to 0.92. The ratio of the diameter of the inner bottom surface 5b to the total width of the internal space 2 is, for example, 0.54 to 0.64. The ratio of the diameter of the upper surface portion 7 to the entire width of the internal space 2 is, for example, 0.12 to 0.36. The ratio of the radius of curvature of the curves 6c and 6C of the inner surface 6s to the total width of the internal space 2 is, for example, 0.62 to 0.74. The curve 6C of the middle portion 2m of the inner surface 6s is, for example, an arc of about 90°. An angle from the horizontal of the upper straight line excluding the curve 6c of the inner side surface 6s and the curve 6C of the intermediate portion 2m of the inner side surface 6s is, for example, 40° to 50° in a cross-sectional view taken along a cross section parallel to the vertical direction. ..

消化槽1Bは、内底面5bから上方に突出した邪魔板20Bを備える。邪魔板20Bは、内底面5bの平坦面5sから上方に突出している。図5(B)に示すように、邪魔板20Bは、平面視で内部空間2の下端部2bの中央部2cに放射状に配置されている。本実施形態では、4枚程度の邪魔板20Bが内底面5bの中心5cを囲繞するように互いに間隔を空けつつ、十字状をなすように放射状に配置されている。邪魔板径dRAD/槽径Dh及び邪魔板突出長L/翼径dの好ましい範囲等の他の事項については、上記第1実施形態の消化槽1Aと同様である。 The digestion tank 1B includes a baffle plate 20B that projects upward from the inner bottom surface 5b. The baffle plate 20B projects upward from the flat surface 5s of the inner bottom surface 5b. As shown in FIG. 5(B), the baffle plate 20B is radially arranged in the central portion 2c of the lower end portion 2b of the internal space 2 in a plan view. In the present embodiment, about four baffle plates 20B are radially arranged in a cross shape while being spaced from each other so as to surround the center 5c of the inner bottom surface 5b. Other matters such as the preferable range of the baffle plate diameter dRAD/tank diameter Dh and the baffle plate protruding length L/blade diameter d are the same as those of the digestion tank 1A of the first embodiment.

本実施形態によれば、被消化物Wを収容する内部空間2の下端部2bを規定する内底面5bを有する底壁5Bと、内部空間2を規定しつつ、内底面5bの周縁部5pから延在し、内部空間2の上端部2u及び下端部2bに至るにつれて内部空間2の中心の側に集束する内側面6sを有する側壁6とを備えた消化槽1Bにおいて、攪拌機構10により内部空間2に収容された被消化物Wが上下方向に平行な軸周りに攪拌され、内底面5bから上方に突出した邪魔板20Bにより、被消化物Wに内部空間2の下端部2bから上方に向う上昇流が形成されることに加えて、内底面5bは内部空間2の上端部2uで側壁6の上縁部6uにより規定された上面部7よりも広い平坦面5sを有し、邪魔板20Bは平坦面5sから上方に突出しており、より速い上昇流が形成され、流動不良部がより生じ難いため、消化槽1Bの内部空間2の全体における被消化物Wの混合の均一性をさらに向上させることができる。 According to the present embodiment, the bottom wall 5B having the inner bottom surface 5b that defines the lower end portion 2b of the inner space 2 that houses the digested material W, and the peripheral portion 5p of the inner bottom surface 5b that defines the inner space 2 are provided. In the digestion tank 1B provided with the side wall 6 that extends and reaches the upper end 2u and the lower end 2b of the internal space 2 and converges toward the center side of the internal space 2, the internal space by the stirring mechanism 10 The digested substance W housed in 2 is agitated around an axis parallel to the vertical direction, and the digested substance W is directed upward from the lower end portion 2b of the internal space 2 by the baffle plate 20B protruding upward from the inner bottom surface 5b. In addition to forming the upward flow, the inner bottom surface 5b has a flat surface 5s wider than the upper surface portion 7 defined by the upper edge portion 6u of the side wall 6 at the upper end portion 2u of the inner space 2, and the baffle plate 20B. Is projected upward from the flat surface 5s, a faster upward flow is formed, and a poor flow portion is less likely to occur, so that the uniformity of the mixture of the digested material W in the entire inner space 2 of the digestion tank 1B is further improved. Can be made.

つまり、図6の内部空間2に実線の矢印で示すように、本実施形態の消化槽1Bでは、上記第1実施形態の消化槽1Aと同様に、内部空間2の下端部2bの中央部2cから上昇流が形成され、内部空間2での流動不良部がみられず、良好な混合の均一性が得られる。また、本実施形態の消化槽1Bでは、内部空間2に被消化物Wの大循環流が形成されており、内部空間2の被消化物Wの全体を一様に攪拌することができる。また、本実施形態の消化槽1Bでは、内部空間2のほとんどの領域で、十分な流速を確保でき、堆積やスカム発生の心配が少ない。 That is, as shown by the solid arrow in the internal space 2 of FIG. 6, in the digestion tank 1B of the present embodiment, the central portion 2c of the lower end portion 2b of the internal space 2 is the same as in the digestion tank 1A of the first embodiment. As a result, an upward flow is formed, a flow failure portion in the internal space 2 is not seen, and good mixing uniformity is obtained. Further, in the digestion tank 1B of the present embodiment, the large circulation flow of the digested substance W is formed in the internal space 2, and the entire digested substance W in the internal space 2 can be uniformly stirred. In addition, in the digestion tank 1B of the present embodiment, a sufficient flow velocity can be secured in most regions of the internal space 2, and there is little concern about accumulation or scum generation.

さらに、本実施形態の消化槽1Bでは、上記第1実施形態の消化槽1Aと比較して、内底面5bの周縁部5pにおいても速い流速を得ることができ、汚泥等の被消化物W中の比重の大きい固形物質等の堆積をさらに防止することができる。加えて、本実施形態の消化槽1Bでは、上記第1実施形態の消化槽1Aと比較して、被消化物Wの大きな循環量を得ることができる。 Furthermore, in the digestion tank 1B of the present embodiment, a higher flow velocity can be obtained in the peripheral portion 5p of the inner bottom surface 5b than in the digestion tank 1A of the first embodiment, and the digested material W such as sludge It is possible to further prevent the accumulation of solid substances having a large specific gravity. In addition, in the digestion tank 1B of the present embodiment, a larger circulation amount of the digested material W can be obtained as compared with the digestion tank 1A of the first embodiment.

(実験例)
以下、本発明の実験例について説明する。実験例1として上記第1実施形態の消化槽1A、実験例2として上記第2実施形態の消化槽1B、比較例1として図2に示した消化槽100及び比較例2として図3に示した消化槽200について、CFD(Computational Fluid Dynamics :数値流体力学)による流体解析が行われた。CFDによる流体解析は、ANSYS社の「ANSYS Fluent 19.0」(商品名)により行われた。消化槽1A、消化槽1B、消化槽100及び消化槽200の容量は、いずれも3000mである。消化槽1Aの直径は16.7mであり、消化槽1Bの直径は17.0mであり、消化槽100の直径は16.7mである。消化槽1Aの被消化物Wの深さは23.95mであり、消化槽1Bの被消化物Wの深さは19.85mであり、消化槽100の被消化物Wの深さは23.9mであり、消化槽200の被消化物Wの深さは23.95mである。
(Experimental example)
Hereinafter, experimental examples of the present invention will be described. As Experimental Example 1, the digestive tank 1A of the first embodiment, as Experimental Example 2 the digestive tank 1B of the second embodiment, as Comparative Example 1 the digestive tank 100 shown in FIG. 2 and as Comparative Example 2 shown in FIG. A fluid analysis by CFD (Computational Fluid Dynamics) was performed on the digestion tank 200. The fluid analysis by CFD was performed by "ANSYS Fluent 19.0" (trade name) of ANSYS. The capacities of the digestion tank 1A, the digestion tank 1B, the digestion tank 100 and the digestion tank 200 are all 3000 m 3 . The diameter of the digestion tank 1A is 16.7 m, the diameter of the digestion tank 1B is 17.0 m, and the diameter of the digestion tank 100 is 16.7 m. The depth of the digested material W in the digestion tank 1A is 23.95 m, the depth of the digested material W in the digestion tank 1B is 19.85 m, and the depth of the digested material W in the digestion tank 100 is 23. It is 9 m, and the depth of the digested material W in the digestion tank 200 is 23.95 m.

消化槽1A、消化槽1B、消化槽100及び消化槽200により被消化物Wの攪拌が行われたときの平均流速が測定された。消化槽1A及び消化槽1Bについて邪魔板20A,20Bの直上部における上昇流の流量が循環量として測定された。内底面5bから邪魔板20A,20Bの直径の0.4倍の高さにおける内部空間2の水平な横断面において、上昇流が生じている領域の面積が求められた。当該領域での上昇流の平均流速と当該領域の面積との積から循環量が算出された。なお、消化槽100については、循環量はドラフトチューブ31の吐出流量の入力設定値と同じ値とした。また、消化槽200については、内部空間2の全体での循環流の評価が困難であるため、循環量の測定から除外された。 The average flow velocity when the digested material W was stirred was measured by the digestion tanks 1A, 1B, 100 and 200. For the digestion tank 1A and the digestion tank 1B, the flow rate of the ascending flow immediately above the baffles 20A and 20B was measured as the circulation amount. In the horizontal cross section of the internal space 2 at a height of 0.4 times the diameter of the baffles 20A and 20B from the inner bottom surface 5b, the area of the region where the upward flow is generated was obtained. The circulation amount was calculated from the product of the average flow velocity of the ascending flow in the region and the area of the region. In the digestion tank 100, the circulation amount was the same as the input set value of the discharge flow rate of the draft tube 31. In addition, the digestion tank 200 was excluded from the measurement of the circulation amount because it is difficult to evaluate the circulation flow in the entire inner space 2.

CFDによる流体解析結果は、消化槽1Aのパドル11の回転数が4.20min−1のときに、内部空間2の被消化物Wの平均流速は0.282m/sであり、最大流速は1.39m/sであり、循環量は4032m/hrであり、動力は2.418kWであり、動力密度は0.806W/mであった。 The fluid analysis result by CFD shows that when the rotation speed of the paddle 11 of the digestion tank 1A is 4.20 min -1 , the average flow velocity of the digested substance W in the internal space 2 is 0.282 m/s, and the maximum flow velocity is 1. It was 0.39 m/s, the circulation rate was 4032 m 3 /hr, the power was 2.418 kW, and the power density was 0.806 W/m 3 .

CFDによる流体解析結果は、消化槽1Bのパドル11の回転数が4.12min−1のときに、内部空間2の被消化物Wの平均流速は0.287m/sであり、最大流速は1.41m/sであり、循環量は5364m/hrであり、動力は2.473kWであり、動力密度は0.824W/mであった。 The fluid analysis result by CFD shows that when the rotation speed of the paddle 11 of the digestion tank 1B is 4.12 min −1 , the average flow velocity of the digested substance W in the internal space 2 is 0.287 m/s, and the maximum flow velocity is 1. The power was 0.41 m/s, the circulation rate was 5364 m 3 /hr, the power was 2.473 kW, and the power density was 0.824 W/m 3 .

CFDによる流体解析結果は、消化槽100のドラフトチューブ31の吐出流量が1500m/hrのときに、内部空間2の被消化物Wの平均流速は0.03m/sであり、最大流速は3.1m/sであり、循環量は上記のようにドラフトチューブ31の吐出流量と同じ1500m/hrであり、動力は11.0kWであり、動力密度は3.667W/mであった。 The fluid analysis result by CFD shows that when the discharge flow rate of the draft tube 31 of the digestion tank 100 is 1500 m 3 /hr, the average flow velocity of the digested substance W in the internal space 2 is 0.03 m/s, and the maximum flow velocity is 3 The circulation rate was 1500 m 3 /hr, which was the same as the discharge flow rate of the draft tube 31 as described above, the power was 11.0 kW, and the power density was 3.667 W/m 3 .

CFDによる流体解析結果は、消化槽200のインペラ41の回転数が9.60min−1のときに、内部空間2の被消化物Wの平均流速は0.171m/sであり、最大流速は3.04m/sであり、動力は2.704kWであり、動力密度は0.901W/mであった。 The fluid analysis result by CFD shows that when the rotation speed of the impeller 41 of the digestion tank 200 is 9.60 min −1 , the average flow velocity of the digested substance W in the internal space 2 is 0.171 m/s, and the maximum flow velocity is 3 The power density was 0.04 m/s, the power was 2.704 kW, and the power density was 0.901 W/m 3 .

これらのCFDによる流体解析結果より、消化槽1A及び消化槽1Bは、最大流速は消化槽100,200よりも遅いものの、平均流速は消化槽100の9倍以上速く、消化槽200よりも60%以上速かった。これは、消化槽1A,1Bは内部空間2の全体で消化槽100,200よりも速い流速が得られたことを意味する。また、消化槽1A及び消化槽1Bは、消化槽100の1/4以下の消費電力であり、消化槽200よりも消費電力が8%以上低減されていた。消化槽1Aと消化槽1Bとの平均流速は同程度であった。しかし、消化槽1Bは、消化槽1Aに比べて循環量が30%以上増大されていた。 From the fluid analysis results by these CFD, although the maximum flow velocity of the digestion tanks 1A and 1B is slower than that of the digestion tanks 100 and 200, the average flow velocity is 9 times or more faster than that of the digestion tank 100 and 60% of that of the digestion tank 200. It was faster than that. This means that the digestion tanks 1A and 1B have a higher flow velocity than the digestion tanks 100 and 200 in the entire inner space 2. In addition, the digestion tank 1A and the digestion tank 1B have power consumption that is ¼ or less that of the digestion tank 100, and the power consumption has been reduced by 8% or more compared to the digestion tank 200. The average flow velocities of the digestion tank 1A and the digestion tank 1B were about the same. However, the digestive tank 1B had a circulation amount increased by 30% or more as compared with the digestive tank 1A.

また、図7に示すように、CFDによる流体解析結果では、実験例1の消化槽1A及び実験例2の消化槽1Bのパドル11の動力に対する内部空間2の被消化物Wの平均流速は、比較例1の消化槽100のドラフトチューブ31の動力に対する内部空間2の被消化物Wの平均流速及び比較例2の消化槽200のインペラ41の動力に対する内部空間2の被消化物Wの平均流速よりも速かった。消化槽1Aと消化槽1Bとのパドル11の動力に対する内部空間2の被消化物Wの平均流速は同程度であった。 Further, as shown in FIG. 7, in the fluid analysis result by CFD, the average flow velocity of the digested material W in the internal space 2 with respect to the power of the paddle 11 of the digestion tank 1A of Experimental Example 1 and the digestion tank 1B of Experimental Example 2 is: Average velocity of the digested material W in the internal space 2 with respect to the power of the draft tube 31 of the digestion tank 100 of Comparative Example 1 and average velocity of the digested material W in the internal space 2 with respect to the power of the impeller 41 of the digestive tank 200 of Comparative Example 2. Was faster than. The average flow velocity of the digested material W in the internal space 2 with respect to the power of the paddle 11 in the digestion tank 1A and the digestion tank 1B was about the same.

図8に示すように、CFDによる流体解析結果では、パドル11の先端の周速度に対する内部空間2の被消化物Wの循環量は、実験例2の消化槽1Bが実験例1の消化槽1Aを上回っていた。図9に示すように、実験例1の消化槽1A及び実験例2の消化槽1Bのパドル11の動力に対する内部空間2の被消化物Wの循環量は、比較例1の消化槽100のドラフトチューブ31の動力に対する内部空間2の被消化物Wの循環量よりも多かった。パドル11の動力に対する内部空間2の被消化物Wの循環量は、実験例2の消化槽1Bが実験例1の消化槽1Aを上回っていた。 As shown in FIG. 8, in the fluid analysis result by CFD, the circulation amount of the digested substance W in the internal space 2 with respect to the peripheral velocity of the tip of the paddle 11 is such that the digestion tank 1B of Experimental Example 2 has a digestion tank 1A of Experimental Example 1. Was over. As shown in FIG. 9, the circulation amount of the digested material W in the internal space 2 with respect to the power of the paddle 11 of the digestion tank 1A of Experimental Example 1 and the digestion tank 1B of Experimental Example 2 is the draft of the digestion tank 100 of Comparative Example 1. It was larger than the circulation amount of the digested material W in the internal space 2 with respect to the power of the tube 31. Regarding the circulation amount of the digested material W in the internal space 2 with respect to the power of the paddle 11, the digestion tank 1B of Experimental Example 2 exceeded the digestion tank 1A of Experimental Example 1.

本発明は、上述した実施形態を始めとして、当業者の知識に基づいて種々の変更、改良を施した様々な形態で実施することができる。また、上述した実施形態に記載されている技術的事項を利用して変形例を構成することも可能である。例えば、上記消化槽1A,1Bでは、卵形の形状を有し、内側面6sは上下方向に平行な断面による断面視で曲線6cを含んでいた。しかし、内側面6sは、例えば、上下方向に平行な断面による断面視で直線のみから構成されていてもよく、消化槽1A,1Bは上下方向に平行な断面による断面視で、上下方向に平行な対辺を有する六角形状の内側面6sを有していてもよい。 The present invention can be implemented in various forms including various modifications and improvements based on the knowledge of those skilled in the art, including the above-described embodiments. Further, it is also possible to configure the modified example by utilizing the technical matters described in the above-mentioned embodiment. For example, in the digestion tanks 1A and 1B, the digestive tanks 1A and 1B have an oval shape, and the inner surface 6s includes a curve 6c in a cross-sectional view in a cross section parallel to the vertical direction. However, the inner surface 6s may be composed of only straight lines in a sectional view in a cross section parallel to the vertical direction, and the digestion tanks 1A and 1B are parallel to the vertical direction in a sectional view parallel to the vertical direction. It may have a hexagonal inner side surface 6s having opposite sides.

1A,1B…消化槽、2…内部空間、2u…上端部、2b…下端部、2c…中央部、2m…中間部、3…外殻、4…台座部、5A,5B…底壁、5b…内底面、5p…周縁部、5s…平坦面、5c…中心、6…側壁、6s…内側面、6u…上縁部、6c…曲線、6C…曲線、7…上面部、10…攪拌機構、11…パドル、12…回転軸、13…駆動部、20A,20B…邪魔板、31…ドラフトチューブ、41…インペラ、42…回転軸、100,200…消化槽、E…地中、W…被消化物、Dh…槽径、d…翼径、dRAD…邪魔板径、L…邪魔板突出長。 1A, 1B... Digestion tank, 2... Internal space, 2u... Upper end part, 2b... Lower end part, 2c... Central part, 2m... Intermediate part, 3... Outer shell, 4... Pedestal part, 5A, 5B... Bottom wall, 5b ... inner bottom surface, 5p... peripheral portion, 5s... flat surface, 5c... center, 6... side wall, 6s... inner side surface, 6u... upper edge portion, 6c... curved line, 6C... curved line, 7... upper surface portion, 10... stirring mechanism , 11... Paddle, 12... Rotating shaft, 13... Drive part, 20A, 20B... Baffle plate, 31... Draft tube, 41... Impeller, 42... Rotating shaft, 100, 200... Digestion tank, E... Underground, W... Digested material, Dh... tank diameter, d... blade diameter, dRAD... baffle plate diameter, L... baffle plate protruding length.

Claims (5)

被消化物を収容する内部空間の下端部を規定する内底面を有する底壁と、
前記内部空間を規定し、前記内底面の周縁部から延在し、前記内部空間の上端部及び下端部に至るにつれて前記内部空間の中心の側に集束する内側面を有する側壁と、
前記内部空間に収容された前記被消化物を上下方向に平行な軸周りに攪拌する攪拌機構と、
前記内底面から上方に突出した邪魔板と、
を備え、
前記内底面は、前記内部空間の上端部で前記側壁の上縁部により規定された上面部よりも広い平坦面を有し、
前記邪魔板は、前記平坦面から上方に突出している、消化槽。
A bottom wall having an inner bottom surface that defines the lower end of the internal space that houses the substance to be digested;
A sidewall having an inner side surface that defines the inner space, extends from the peripheral edge of the inner bottom surface, and converges toward the center of the inner space as it reaches the upper end and the lower end of the inner space,
A stirring mechanism for stirring the digested material contained in the internal space around an axis parallel to the vertical direction,
A baffle protruding upward from the inner bottom surface,
Equipped with
The inner bottom surface has a flat surface wider than an upper surface portion defined by an upper edge portion of the side wall at an upper end portion of the internal space,
The baffle plate is a digestive tank that protrudes upward from the flat surface.
前記邪魔板は、平面視で前記内部空間の下端部の中央部に放射状に配置されている、請求項に記載の消化槽。 The digestive tank according to claim 1 , wherein the baffle plate is radially arranged in a central portion of a lower end portion of the internal space in a plan view. 前記攪拌機構は、上下方向に平行なパドルと、前記パドルを上下方向に平行な軸周りに回転させる回転軸とを有する、請求項1又は2に記載の消化槽。 The digestion tank according to claim 1 or 2 , wherein the stirring mechanism has a paddle that is parallel to the vertical direction and a rotation shaft that rotates the paddle about an axis that is parallel to the vertical direction. 前記内側面は、上下方向に平行な断面による断面視で曲線を含む、請求項1〜のいずれか1項に記載の消化槽。 The inner surface comprises a curved when viewed in section according to a cross section parallel to the vertical direction, digester according to any one of claims 1-3. 前記内側面は、上下方向に平行な断面による断面視で、前記内部空間の上端部と下端部との上下方向の距離とが等しい中間部で、前記内部空間の上端部及び下端部に至るにつれて前記内部空間の中心の側に集束する曲線を含む、請求項1〜のいずれか1項に記載の消化槽。 The inner surface is an intermediate portion where the vertical distance between the upper end and the lower end of the internal space is the same in a cross-sectional view taken along a cross section parallel to the vertical direction, and as the upper end and the lower end of the internal space are reached. The digestive tank according to any one of claims 1 to 5 , comprising a curve that converges toward the center side of the internal space.
JP2019223909A 2019-12-11 2019-12-11 Digestive tank Active JP6733928B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2019223909A JP6733928B1 (en) 2019-12-11 2019-12-11 Digestive tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2019223909A JP6733928B1 (en) 2019-12-11 2019-12-11 Digestive tank

Publications (2)

Publication Number Publication Date
JP6733928B1 true JP6733928B1 (en) 2020-08-05
JP2021090926A JP2021090926A (en) 2021-06-17

Family

ID=71892260

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2019223909A Active JP6733928B1 (en) 2019-12-11 2019-12-11 Digestive tank

Country Status (1)

Country Link
JP (1) JP6733928B1 (en)

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6024395U (en) * 1983-07-22 1985-02-19 月島機械株式会社 Scum generation prevention device
JPS6190728A (en) * 1984-10-08 1986-05-08 Taisei Corp Stirring method of inside of tank
JPH02131198A (en) * 1988-11-10 1990-05-18 Nkk Corp Agitating device for digestion tank in sludge treatment equipment
JPH02144200A (en) * 1988-11-26 1990-06-01 Nkk Corp Digestion tank in sludge treating equipment
JP2976772B2 (en) * 1993-09-28 1999-11-10 日本鋼管株式会社 Operation method of digestion tank
JP3294130B2 (en) * 1996-12-04 2002-06-24 古河機械金属株式会社 Digestion tank mechanical stirrer
JPH10290999A (en) * 1997-04-22 1998-11-04 Nkk Corp Agitator of digestion tank
JP2004105798A (en) * 2002-09-13 2004-04-08 Jfe Engineering Kk Digestion tank
JP6503253B2 (en) * 2015-07-28 2019-04-17 メタウォーター株式会社 Stirring method of anaerobic fermentation tank

Also Published As

Publication number Publication date
JP2021090926A (en) 2021-06-17

Similar Documents

Publication Publication Date Title
US3479017A (en) Apparatus for charging liquids with gases
US8277114B2 (en) Gas foil impeller
JPS5922633A (en) Method and apparatus for mixing gas and liquid
WO2017185431A1 (en) Gas-liquid dispersion mixing device equipped with annular sector-shaped concave surface impeller blade
JP3632827B2 (en) Stirrer
KR101822334B1 (en) Defoamer for fermenter, and microorganism fermenter using defoamer
CN102068955A (en) Flocculation reactor with special-shaped spoiler
US20190374913A1 (en) Stirred tank
KR20030013247A (en) Aerating and stirring apparatus
TWI727700B (en) Mixing blade assembly and mixing tank
JP2019198813A (en) Agitation device
JP6733928B1 (en) Digestive tank
JP2013248565A (en) Sludge flocculation device, and method for conditioning sludge
JP3578782B2 (en) Stirrer
JP2015514569A (en) Impeller of stirring device and stirring device using the same
US6030113A (en) Mixing apparatus and method for mixing black liquor from cellulose production with ash from flue gases formed from combustion of black liquor
JP2018089558A (en) Crystallization reaction bath, and crystallization reaction classifier using the reaction bath
JPWO2011048698A1 (en) Stirrer
JP6714254B2 (en) Moist air flow generator
KR101767500B1 (en) Impeller for digestion tank agitator
JP4316251B2 (en) Closed stirring device
KR102300428B1 (en) High-efficiency mixed magnetic impeller stirrer using sediment suppression and multiple vortices
JPH03267136A (en) Vertical type stirrer
JPH07786A (en) Impeller
KR102019631B1 (en) Underwater stirring device with sludge circulation stirring structure

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20200110

A871 Explanation of circumstances concerning accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A871

Effective date: 20200110

A975 Report on accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A971005

Effective date: 20200115

A871 Explanation of circumstances concerning accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A871

Effective date: 20200130

A975 Report on accelerated examination

Free format text: JAPANESE INTERMEDIATE CODE: A971005

Effective date: 20200205

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20200331

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20200427

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20200623

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20200702

R150 Certificate of patent or registration of utility model

Ref document number: 6733928

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250