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JP5680938B2 - Water-containing organic matter drying equipment - Google Patents
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JP5680938B2 - Water-containing organic matter drying equipment - Google Patents

Water-containing organic matter drying equipment Download PDF

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JP5680938B2
JP5680938B2 JP2010254060A JP2010254060A JP5680938B2 JP 5680938 B2 JP5680938 B2 JP 5680938B2 JP 2010254060 A JP2010254060 A JP 2010254060A JP 2010254060 A JP2010254060 A JP 2010254060A JP 5680938 B2 JP5680938 B2 JP 5680938B2
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water
containing organic
inner cylinder
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organic matter
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JP2012102976A (en
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難波 昌洋
昌洋 難波
富孝 外山
富孝 外山
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株式会社まさなみ鉄工
株式会社エム・イ−・ティ−
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    • 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

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  • Treatment Of Sludge (AREA)

Description

本発明は、汚泥や生ゴミや畜産廃棄物などの含水有機物を乾燥するための乾燥装置に関する。   The present invention relates to a drying apparatus for drying water-containing organic matter such as sludge, raw garbage, and livestock waste.

汚泥などの含水有機物を乾燥するための乾燥装置としては、その中心軸が略水平に配された筒状のケーシング(外筒)と、該外筒内に収容されて前記中心軸と略平行な軸周りに回転する撹拌翼とを備えたもの(以下においては、説明の便宜上、「撹拌翼回転型の乾燥装置」と呼ぶことがある。)が知られている(例えば、特許文献1〜5)。撹拌翼回転型の乾燥装置では、乾燥対象である含水有機物を前方から前記外筒内へと導入し、前記外筒内の含水有機物を前記撹拌翼で撹拌しながら外筒内へ熱風を入れることにより含水有機物の乾燥を行うものとなっている。これにより、含水有機物が外筒や撹拌翼などに粘着しないようにすることができる。乾燥された含水有機物は、前記撹拌翼、あるいはその他の送り出し手段により、外筒の後方へと送出される。   As a drying apparatus for drying water-containing organic matter such as sludge, a cylindrical casing (outer cylinder) whose central axis is arranged substantially horizontally, and accommodated in the outer cylinder and substantially parallel to the central axis There is known one having an agitating blade rotating around an axis (hereinafter, sometimes referred to as “agitating blade rotating type drying device” for convenience of explanation) (for example, Patent Documents 1 to 5). ). In the stirring blade rotating type drying apparatus, water-containing organic matter to be dried is introduced into the outer cylinder from the front, and hot air is put into the outer cylinder while stirring the water-containing organic matter in the outer cylinder with the stirring blade. Thus, the water-containing organic matter is dried. Thereby, it is possible to prevent the water-containing organic matter from sticking to the outer cylinder, the stirring blade, or the like. The dried water-containing organic matter is sent to the rear of the outer cylinder by the stirring blade or other delivery means.

しかし、従来の撹拌翼回転型の乾燥装置では、前記外筒内に導入された含水有機物の全体を前記撹拌翼で粉砕しながら乾燥させる必要があった。このため、前記撹拌翼の回転径は、前記外筒の内径と同じ程度の大きなものにしなければならず、従来の撹拌翼回転型の乾燥装置は、前記撹拌翼の回転に大きな駆動力を要するものとなっていた。前記撹拌翼の駆動力は、下水汚泥や家畜糞など、含水有機物の粘性が高くなればなるほど大きくする必要がある。しかし、それでもなお、従来の撹拌翼回転型の乾燥装置では、前方から前記外筒内に導入された含水有機物が粘性を保ったまま大きな塊状となって外筒内へ落下することもあり、前記外筒内における前端部付近の内底面に滞留するおそれもあった。このため、前記撹拌翼が回転しなくなるなどの不具合も生じやすかった。   However, in the conventional stirring blade rotating type drying apparatus, it was necessary to dry the entire water-containing organic substance introduced into the outer cylinder while pulverizing with the stirring blade. For this reason, the rotating diameter of the stirring blade must be as large as the inner diameter of the outer cylinder, and the conventional stirring blade rotating type drying apparatus requires a large driving force to rotate the stirring blade. It was a thing. The driving force of the stirring blade needs to be increased as the viscosity of the water-containing organic matter such as sewage sludge and livestock dung becomes higher. However, in the conventional stirring blade rotating type drying apparatus, the water-containing organic matter introduced into the outer cylinder from the front may fall into a large lump while maintaining the viscosity, There was also a risk of staying on the inner bottom surface near the front end in the outer cylinder. For this reason, problems such as the stirring blades not rotating easily occur.

特開平08−010989号公報Japanese Patent Laid-Open No. 08-010989 特開平09−001197号公報JP 09-001197 A 特開平10−148471号公報JP-A-10-148471 特開2007−136348号公報JP 2007-136348 A 特開2008−173551号公報JP 2008-173551 A

本発明は、上記課題を解決するためになされたものであり、外筒内に投入されたばかりの含水有機物が外筒内における前端部付近に落下して粘着するのを防ぐことにより、撹拌翼が回転しなくなるなどの不具合の発生を抑えることができ、含水有機物を効率的に乾燥することのできる含水有機物の乾燥装置を提供するものである。また、従来の撹拌翼回転型の乾燥装置と比較して、撹拌翼などの回転の駆動力を小さくすることができる含水有機物の乾燥装置を提供することも本発明の目的である。   The present invention has been made in order to solve the above problems, and prevents the water-containing organic material just put into the outer cylinder from dropping and sticking to the vicinity of the front end in the outer cylinder. It is an object of the present invention to provide a water-containing organic matter drying apparatus that can suppress the occurrence of problems such as no longer rotating and can efficiently dry water-containing organic matter. Another object of the present invention is to provide a water-containing organic matter drying device capable of reducing the rotational driving force of a stirring blade or the like as compared with a conventional stirring blade rotating type drying device.

上記課題は、その中心軸が前後方向に向けられた外筒と、外筒内に収容されて外筒の中心軸に沿って配された内筒と、外筒の前方から外筒内へと含水有機物を供給し、含水有機物を内筒の外周面上へ落下させる含水有機物供給手段と、内筒を加熱する内筒加熱手段と、内筒をその中心軸周りに回転させる内筒回転手段と、外筒内へ供給されて内筒の外周面上へ落下する前の含水有機物を両側から押圧する少なくとも一対の押圧ローラと、それぞれの押圧ローラをその中心軸周りに回転させる押圧ローラ回転手段と、を備え、含水有機物供給手段によって外筒内へ供給された含水有機物を押圧ローラで板状に成形してから内筒の外周面上へと落下させ、該含水有機物を内筒で熱しながら外筒の後方へ移送することができるようにしたことを特徴とする含水有機物の乾燥装置を提供することによって解決される。   The above-described problems include an outer cylinder whose central axis is directed in the front-rear direction, an inner cylinder accommodated in the outer cylinder and disposed along the central axis of the outer cylinder, and from the front of the outer cylinder to the outer cylinder. Water-containing organic matter supplying means for supplying water-containing organic matter and dropping the water-containing organic matter onto the outer peripheral surface of the inner cylinder, inner cylinder heating means for heating the inner cylinder, and inner cylinder rotating means for rotating the inner cylinder around its central axis At least a pair of pressing rollers for pressing the water-containing organic matter from both sides before being supplied into the outer cylinder and falling onto the outer peripheral surface of the inner cylinder; and a pressing roller rotating means for rotating each pressing roller around its central axis The water-containing organic substance supplied into the outer cylinder by the water-containing organic substance supply means is formed into a plate shape with a pressing roller and then dropped onto the outer peripheral surface of the inner cylinder, and the water-containing organic substance is heated while being heated by the inner cylinder. It is possible to transfer to the rear of the cylinder It is solved by providing a drying device of the hydrous organic matter.

このように、外筒内へ供給された含水有機物を押圧ローラで板状に成形してからその下方の内筒へ落下させて熱するようにすることにより、含水有機物の表面積を増大させてその表面の水分を蒸発しやすくし、含水有機物が乾燥装置の各部に粘着しないようにすることが可能になる。このため、含水有機物が後述する撹拌翼の回転を阻害しないようにして、含水有機物を外筒内で後方へ確実に移送させることも可能になる。したがって、後述する撹拌翼の回転に要する駆動力を小さく抑えることも可能である。乾燥装置の投入初期段階において、含水有機物の少なくとも表面の含水率を50〜60%程度まで低下させることができれば、含水有機物の粘着を防止することができる。   In this way, the water-containing organic substance supplied into the outer cylinder is formed into a plate shape with a pressing roller and then dropped into the inner cylinder below it to heat, thereby increasing the surface area of the water-containing organic substance. It is possible to easily evaporate the water on the surface and prevent the water-containing organic matter from sticking to each part of the drying apparatus. For this reason, it is also possible to reliably transfer the water-containing organic matter backward in the outer cylinder so that the water-containing organic matter does not hinder the rotation of the stirring blade described later. Therefore, it is possible to suppress the driving force required for the rotation of the stirring blade described later. If the moisture content of at least the surface of the water-containing organic substance can be reduced to about 50 to 60% at the initial stage of the input of the drying apparatus, sticking of the water-containing organic substance can be prevented.

本発明の含水有機物の乾燥装置において、内筒加熱手段は、内筒を加熱できるものであれば特に限定されない。しかし、内筒加熱手段を、内筒の後方から内筒内へと熱風を送り込む熱風発生手段とすると好ましい。これにより、内筒全体を効率的に加熱することが可能になる。このとき、内筒の周壁に該周壁を内外に連通する複数の通気孔を設け、熱風発生手段によって内筒内へ送り込まれた熱風が前記連通孔を通じて内筒外へ抜け出るようにすると好ましい。これにより、外筒内へ供給された含水有機物は、内筒によって直接的に焼かれるだけでなく、前記連通孔を通じて内筒外へ抜け出てきた熱風(熱気)によっても加熱されるようになる。また、外筒内へ供給された含水有機物を熱風によってさらに撹拌することも可能になる。したがって、含水有機物をより効率的に乾燥させることが可能になる。   In the water-containing organic matter drying apparatus of the present invention, the inner cylinder heating means is not particularly limited as long as it can heat the inner cylinder. However, it is preferable that the inner cylinder heating means be hot air generating means for sending hot air from the rear of the inner cylinder into the inner cylinder. Thereby, it becomes possible to heat the whole inner cylinder efficiently. At this time, it is preferable to provide a plurality of vent holes in the peripheral wall of the inner cylinder so as to communicate the peripheral wall inward and outward so that the hot air sent into the inner cylinder by the hot air generating means escapes to the outside of the inner cylinder through the communication hole. Thereby, the water-containing organic substance supplied into the outer cylinder is not only directly baked by the inner cylinder, but also heated by hot air (hot air) that has flowed out of the inner cylinder through the communication hole. It is also possible to further stir the hydrated organic substance supplied into the outer cylinder with hot air. Therefore, it becomes possible to dry a water-containing organic substance more efficiently.

また、本発明の含水有機物の乾燥装置において、押圧ローラは、特に加熱をしなくても構わないが、含水有機物の再粘着をさらに確実に防いで含水有機物をより効率的に乾燥するためには、内筒と同様、押圧ローラも加熱すると好ましい。この場合、押圧ローラは、内筒加熱手段を利用して加熱するようにしてもよいが、押圧ローラを加熱するための押圧ローラ加熱手段を内筒加熱手段とは独立して設けると好ましい。これにより、外筒内に供給されたばかりの含水有機物を押圧ローラでより高温で加熱することが可能になり、含水有機物をより効率的に乾燥することが可能になる。   Further, in the water-containing organic matter drying apparatus of the present invention, the pressing roller does not need to be heated in particular, but in order to more reliably prevent the water-containing organic matter from re-adhering and more efficiently dry the water-containing organic matter. As with the inner cylinder, it is preferable to heat the pressure roller. In this case, the pressure roller may be heated using the inner cylinder heating means, but it is preferable to provide the pressure roller heating means for heating the pressure roller independently from the inner cylinder heating means. Thereby, it becomes possible to heat the water-containing organic material just supplied into the outer cylinder at a higher temperature with the pressing roller, and it becomes possible to dry the water-containing organic material more efficiently.

さらに、本発明の含水有機物の乾燥装置において、外筒をその中心軸周りに回転させる外筒回転手段を設けるとともに、内筒の外周面から落下してきた含水有機物を外筒内の上部へとかき揚げるための撹拌翼を外筒の内周面から内向きに設けることも好ましい。このように外筒自体を回転させることにより、含水有機物をより効率的に撹拌するだけでなく、外筒内における前端部付近に含水有機物が滞留するのをより確実に防ぐことが可能になる。   Further, in the water-containing organic matter drying apparatus of the present invention, an outer cylinder rotating means for rotating the outer cylinder around its central axis is provided, and the organic water that has fallen from the outer peripheral surface of the inner cylinder is lifted up to the upper part in the outer cylinder. It is also preferable to provide a stirring blade for inward from the inner peripheral surface of the outer cylinder. Thus, by rotating the outer cylinder itself, it is possible not only to stir the water-containing organic substance more efficiently but also more reliably prevent the water-containing organic substance from staying in the vicinity of the front end portion in the outer cylinder.

以上のように、本発明によって、外筒内に投入されたばかりの含水有機物が外筒内における前端部付近に落下して粘着するのを防ぐことにより、撹拌翼が回転しなくなるなどの不具合の発生を抑えることができ、含水有機物を効率的に乾燥することのできる含水有機物の乾燥装置を提供することが可能になる。また、従来の撹拌翼回転型の乾燥装置と比較して、撹拌翼などの回転の駆動力を小さくすることができる含水有機物の乾燥装置を提供することも可能になる。   As described above, according to the present invention, it is possible to prevent the water-containing organic material just put into the outer cylinder from dropping and sticking to the vicinity of the front end in the outer cylinder, thereby causing the occurrence of problems such as the stirring blade not rotating. Therefore, it is possible to provide a water-containing organic matter drying apparatus that can efficiently dry the water-containing organic matter. It is also possible to provide a water-containing organic matter drying device capable of reducing the rotational driving force of the stirring blade or the like as compared with a conventional stirring blade rotating type drying device.

本発明の含水有機物の乾燥装置を外筒の中心軸を含む鉛直面で切断した状態を示した断面図である。It is sectional drawing which showed the state which cut | disconnected the drying apparatus of the water-containing organic substance of this invention by the vertical plane containing the central axis of an outer cylinder. 本発明の含水有機物の乾燥装置における外筒をその中心軸に垂直な鉛直面(図1におけるA−A面)で切断した状態を示した断面図である。It is sectional drawing which showed the state which cut | disconnected the outer cylinder in the drying apparatus of the water-containing organic substance of this invention by the perpendicular surface (AA surface in FIG. 1) perpendicular | vertical to the central axis.

0.含水有機物の乾燥装置の概要
本発明の含水有機物の乾燥装置の好適な実施態様について、図面を用いてより具体的に説明する。図1は、本発明の含水有機物の乾燥装置を外筒10の中心軸を含む鉛直面で切断した状態を示した断面図である。図2は、本発明の含水有機物の乾燥装置における外筒10をその中心軸に垂直な鉛直面(図1におけるA−A面)で切断した状態を示した断面図である。
0. Outline of Hydrous Organic Drying Apparatus A preferred embodiment of the hydrous organic drying apparatus of the present invention will be described more specifically with reference to the drawings. FIG. 1 is a cross-sectional view showing a state in which the water-containing organic matter drying apparatus of the present invention is cut along a vertical plane including the central axis of the outer cylinder 10. FIG. 2 is a cross-sectional view showing a state in which the outer cylinder 10 in the water-containing organic matter drying apparatus of the present invention is cut along a vertical plane (A-A plane in FIG. 1) perpendicular to the central axis.

本実施態様の含水有機物の乾燥装置は、図1に示すように、その中心軸が前後方向に向けられた外筒10と、外筒10をその中心軸周りに回転させる外筒回転手段20と、外筒10内に収容されて外筒10の中心軸に沿って配された内筒30と、外筒10の前方から外筒10内へと含水有機物を供給し、含水有機物を内筒30の外周面上へ落下させる含水有機物供給手段40と、内筒30を加熱する内筒加熱手段50と、内筒30をその中心軸周りに回転させる内筒回転手段60と、外筒10内へ供給されて内筒30の外周面上へ落下する前の含水有機物を両側から押圧する少なくとも一対の押圧ローラ70と、押圧ローラ70を加熱する押圧ローラ加熱手段80と、それぞれの押圧ローラ70をその中心軸周りに回転させる押圧ローラ回転手段90とを備えたものとなっている。この含水有機物の乾燥装置において、含水有機物供給手段40によって外筒10内へ供給された含水有機物は、押圧ローラ70で板状に成形されてから内筒30の外周面上へと落下し、内筒30で熱されながら外筒10の後方へ移送される。   As shown in FIG. 1, the water-containing organic matter drying apparatus of the present embodiment includes an outer cylinder 10 whose central axis is directed in the front-rear direction, and an outer cylinder rotating unit 20 that rotates the outer cylinder 10 around the central axis. The inner cylinder 30 accommodated in the outer cylinder 10 and arranged along the central axis of the outer cylinder 10, the water-containing organic substance is supplied from the front of the outer cylinder 10 into the outer cylinder 10, and the water-containing organic substance is supplied to the inner cylinder 30. Water-containing organic substance supplying means 40 for dropping onto the outer peripheral surface of the inner cylinder, inner cylinder heating means 50 for heating the inner cylinder 30, inner cylinder rotating means 60 for rotating the inner cylinder 30 about its central axis, and into the outer cylinder 10 At least a pair of pressing rollers 70 that press the water-containing organic matter before being dropped onto the outer peripheral surface of the inner cylinder 30 from both sides, a pressing roller heating means 80 that heats the pressing rollers 70, and each pressing roller 70 are Rotating pressure roller that rotates around the central axis It has become a thing that includes a stage 90. In this water-containing organic matter drying apparatus, the water-containing organic material supplied into the outer cylinder 10 by the water-containing organic material supply means 40 is formed into a plate shape by the pressing roller 70 and then falls onto the outer peripheral surface of the inner cylinder 30, It is transferred to the rear of the outer cylinder 10 while being heated by the cylinder 30.

1.外筒
本実施態様の含水有機物の乾燥装置において、外筒10は、略円筒状のものとなっており、図1に示すように、その中心軸が水平となっているが、外筒10の中心軸は、水平から傾斜させてもよい。この場合、含水有機物が供給される外筒10の前端側が、含水有機物が送出される外筒10の後端側よりも高くなるようにしておくと好ましい。これにより、外筒10へ供給された含水有機物が外筒10内をさらに後方へ移送しやすくなり、外筒10内における所定箇所に含水有機物がさらに滞留しにくくすることができる。外筒10の中心軸を傾斜させる場合、その傾斜角度は、特に限定されない。しかし、外筒10の傾斜角度を小さくしすぎると、外筒10を傾斜させる意味がなくなるし、外筒10の傾斜角度を大きくしすぎると、外筒10内の前端部へ導入された含水有機物が外筒10内の後端部へ滑り落ちるようになるおそれがある。このため、外筒10を傾斜させる場合には、外筒10の傾斜角度は、通常、1〜50°、好ましくは3〜40°、より好ましくは、5〜30°とされる。
1. Outer cylinder In the water-containing organic matter drying apparatus of the present embodiment, the outer cylinder 10 has a substantially cylindrical shape, and its central axis is horizontal as shown in FIG. The central axis may be inclined from the horizontal. In this case, it is preferable that the front end side of the outer cylinder 10 to which the water-containing organic substance is supplied be higher than the rear end side of the outer cylinder 10 to which the water-containing organic substance is delivered. Thereby, the water-containing organic substance supplied to the outer cylinder 10 can be more easily transferred backward in the outer cylinder 10, and the water-containing organic substance can be further prevented from staying at a predetermined location in the outer cylinder 10. When the central axis of the outer cylinder 10 is inclined, the inclination angle is not particularly limited. However, if the inclination angle of the outer cylinder 10 is too small, there is no point in inclining the outer cylinder 10, and if the inclination angle of the outer cylinder 10 is too large, the water-containing organic substance introduced into the front end portion in the outer cylinder 10 May slide down to the rear end of the outer cylinder 10. For this reason, when the outer cylinder 10 is inclined, the inclination angle of the outer cylinder 10 is normally 1 to 50 °, preferably 3 to 40 °, and more preferably 5 to 30 °.

また、本実施態様の含水有機物の乾燥装置において、外筒10の内周面には、図1と図2に示すように、撹拌翼11を内向きに設けている。この撹拌翼11によって、内筒30の外周面から外筒10の下側の内周面へ落下してきた含水有機物を外筒10内の上部へ再びかき揚げることができるようになっている。本実施態様の含水有機物の乾燥装置においては、図2に示すように、外筒10の中心軸に対して回転対称となるように4本の撹拌翼11を設けている。それぞれの撹拌翼11は、図1に示すように、外筒10の内周面の周方向へ連続的に場所を変えながら外筒10の中心軸方向に延びており、全体としては螺旋状を為している。このため、外筒10をその中心軸回りに回転させると、外筒10と一体的にそれぞれの撹拌翼11も回転するようになっており、後述する撹拌翼31と相俟って含水有機物を後方へと送ることができるようになっている。撹拌翼11や撹拌翼31の枚数や寸法は、後述する充填率を維持できるように、適宜決定する。   Further, in the water-containing organic matter drying apparatus of the present embodiment, a stirring blade 11 is provided inward on the inner peripheral surface of the outer cylinder 10 as shown in FIGS. 1 and 2. With the stirring blade 11, the water-containing organic matter that has fallen from the outer peripheral surface of the inner cylinder 30 to the inner peripheral surface of the outer cylinder 10 can be raked up again in the upper part of the outer cylinder 10. In the water-containing organic matter drying apparatus of this embodiment, as shown in FIG. 2, four stirring blades 11 are provided so as to be rotationally symmetrical with respect to the central axis of the outer cylinder 10. As shown in FIG. 1, each stirring blade 11 extends in the central axis direction of the outer cylinder 10 while continuously changing the position in the circumferential direction of the inner peripheral surface of the outer cylinder 10, and as a whole has a spiral shape. I'm doing it. For this reason, when the outer cylinder 10 is rotated around its central axis, the respective stirring blades 11 are also rotated integrally with the outer cylinder 10, and the water-containing organic matter is combined with the stirring blades 31 described later. It can be sent backwards. The number and dimensions of the stirring blades 11 and the stirring blades 31 are appropriately determined so that the filling rate described later can be maintained.

外筒10の内半径(撹拌翼11を除いた内周面の半径。以下、内半径Rとする。)など、外筒10の寸法は、外筒10の乾燥有効体積などを考慮して適宜決定する。外筒10の乾燥有効体積の計算方法は、以下の通りである。 (Radius of the inner peripheral surface excluding the stirring blade 11. Hereinafter, the inner radius R 1.) Inner radius of the outer cylinder 10, such as the dimensions of the outer cylinder 10, in consideration of drying the effective volume of the outer cylinder 10 Determine as appropriate. The calculation method of the dry effective volume of the outer cylinder 10 is as follows.

1時間当たりの含水有機物の供給重量をW[kg/h]とし、乾燥前の含水有機物の含水率をαとし、乾燥後の含水有機物の含水率をβとすると、蒸発させるべき水分の重量W[kg/h]は、下記式1で表わされる。

={(α−β)/(1−β)}×W ・・・式1
The weight of water to be evaporated, where W 1 [kg / h] is the supply weight of water-containing organic matter per hour, α is the water content of the water-containing organic material before drying, and β is the water content of the water-containing organic material after drying. W 2 [kg / h] is represented by the following formula 1.

W 2 = {(α−β) / (1-β)} × W 1 Formula 1

また、水の蒸発潜熱をX[kcal/kg]とし、水蒸気の比熱をc[kcal/kg℃]とし、含水有機物における非水成分(乾燥成分)の温度をT[℃]とすると、W[kg/h]の水分を蒸発させるのに必要な蒸発潜熱Q[kcal/h]は、下記式2で表わされる。

=W×(X+c×T) ・・・式2
Also, if the latent heat of vaporization of water is X 1 [kcal / kg], the specific heat of water vapor is c 1 [kcal / kg ° C.], and the temperature of the non-aqueous component (dry component) in the water-containing organic matter is T [° C.] The latent heat of vaporization Q 1 [kcal / h] necessary for evaporating water of W 2 [kg / h] is expressed by the following formula 2.

Q 1 = W 2 × (X 1 + c 1 × T) Equation 2

さらに、蒸発潜熱をX[kcal/kg]とすると、含水有機物の乾燥成分の持出熱量Q[kcal/h]は、下記式3で表わされる。

=(W−W)×X ・・・式3
Further, assuming that the latent heat of vaporization is X 2 [kcal / kg], the amount of heat carried out Q 2 [kcal / h] of the dry component of the water-containing organic material is expressed by the following formula 3.

Q 2 = (W 1 −W 2 ) × X 2 Formula 3

さらにまた、1時間当たりに必要な熱量Q[kcal/h]は、下記式4で表わされる。

=Q+Q ・・・式4
Furthermore, the amount of heat Q 3 [kcal / h] required per hour is expressed by the following formula 4.

Q 3 = Q 1 + Q 2 ... Formula 4

そして、外筒10の対数平均温度差をΔT[℃]とすると、「乾燥装置の単位有効体積における水の蒸発能力」を表わす熱容量係数をC[kcal/mh℃]とするために必要な外筒10の乾燥有効体積V[m]は、下記式5で求めることができる。

=(Q/ΔT)/C ・・・式5

上記式5における熱容量係数Cは、できるだけ大きく設定する必要があり、一般的には、150[kcal/mh℃]程度に設定される。
When the logarithmic average temperature difference of the outer cylinder 10 is ΔT [° C.], it is necessary to set the heat capacity coefficient representing the “water evaporation capacity in the unit effective volume of the drying apparatus” to C [kcal / m 3 h ° C.]. The dry effective volume V 1 [m 3 ] of the outer cylinder 10 can be obtained by the following formula 5.

V 1 = (Q 3 / ΔT) / C Equation 5

The heat capacity coefficient C in Equation 5 needs to be set as large as possible, and is generally set to about 150 [kcal / m 3 h ° C.].


具体的に、供給重量Wを4,000[kg/h]とし、含水率αを0.8とし、含水率βを0.3としてみると、重量Wは、上記式1より、2,857[kg/h]と求められる。さらに、蒸発潜熱Xを540[kcal/kg]とし、比熱cを0.47[kcal/kg℃]とし、温度Tを100[℃]とすると、蒸発潜熱Qは、上記式2より、1,677,059[kcal/h]と求められる。さらにまた、Xを100[kcal/kg]とすると、熱量Qは、上記式3より、114,300[kcal/h]と求められる。したがって、熱量Qは、上記式4より、114,300[kcal/h]と求められる。そして、対数平均温度差ΔTを350[℃]とし、熱容量係数Cを150[kcal/mh℃]とすると、乾燥有効体積Vは、上記式5より、34[m]と求められる。したがって、このような条件下で、外筒10の軸方向の長さを11mとした場合には、内筒30の体積を無視すれば、外筒の内半径Rを1m程度とすればよい。

Specifically, when the supply weight W 1 is 4,000 [kg / h], the water content α is 0.8, and the water content β is 0.3, the weight W 2 is 2 857 [kg / h]. Further, when the latent heat of vaporization X 1 is 540 [kcal / kg], the specific heat c 1 is 0.47 [kcal / kg ° C.], and the temperature T is 100 [° C.], the latent heat of vaporization Q 1 is 1,677,059 [kcal / h]. Furthermore, assuming that X 2 is 100 [kcal / kg], the heat quantity Q 2 is obtained as 114,300 [kcal / h] from the above equation 3. Therefore, the amount of heat Q 2 are the above equation 4 is obtained as 114,300 [kcal / h]. When the logarithmic average temperature difference ΔT is 350 [° C.] and the heat capacity coefficient C is 150 [kcal / m 3 h ° C.], the dry effective volume V 1 is calculated as 34 [m 3 ] from the above equation 5. . Therefore, if the axial length of the outer cylinder 10 is 11 m under such conditions, the inner radius R 1 of the outer cylinder may be about 1 m if the volume of the inner cylinder 30 is ignored. .

ところで、上記段落で具体的に計算した条件下で、含水有機物の外筒10内での滞留時間を40分とすると、充填率(外筒10の乾燥有効体積Vに占める含水有機物の体積Vの比率)は17.6%となる。この充填率を大きくしすぎると、外筒10内で含水有機物を効率的に乾燥できなくなるおそれがあるために、通常、30%以下とされる。充填率は、25%以下であると好ましく、20%以下であるとより好ましい。一方、充填率を小さくしすぎると、外筒10の寸法が無駄に大きくなる。このため、充填率は、通常、5%以上、好ましくは10%以上とされる。 By the way, assuming that the residence time of the water-containing organic substance in the outer cylinder 10 is 40 minutes under the conditions specifically calculated in the above paragraph, the filling rate (the volume V of the water-containing organic substance occupying the dry effective volume V 1 of the outer cylinder 10). 2 ) is 17.6%. If the filling rate is increased too much, the water-containing organic matter may not be efficiently dried in the outer cylinder 10, so that the filling rate is usually 30% or less. The filling rate is preferably 25% or less, and more preferably 20% or less. On the other hand, if the filling rate is too small, the dimensions of the outer cylinder 10 become unnecessarily large. For this reason, the filling rate is usually 5% or more, preferably 10% or more.

2.外筒回転手段
外筒回転手段20は、外筒10をその中心軸回りに回転できるものであれば特に限定されない。外筒回転手段20としては、通常、モーターが採用される。外筒回転手段20は、外筒10の中心軸(回転軸)を直接的に回転するように構成してもよいし、ベルトやチェーンなどの機構を用いて間接的に回転するように構成してもよい。外筒10を回転させる向きは、撹拌翼11の向きや内筒30の回転する向きなどに応じて、含水有機物を撹拌しやすく後方へ移送しやすい向きに設定する。本実施態様の含水有機物の製造方法において、外筒10は、図2に示す矢印aの向きに回転するようになっており、撹拌翼11の先端が傾斜した向きへ回転するようにしている。これにより、撹拌翼11によって含水有機物を効率的にかき揚げることが可能となっている。外筒10の回転速度は、上述した充填率を維持できるように適宜決定する。
2. Outer cylinder rotating means The outer cylinder rotating means 20 is not particularly limited as long as it can rotate the outer cylinder 10 around its central axis. As the outer cylinder rotating means 20, a motor is usually employed. The outer cylinder rotating means 20 may be configured to directly rotate the central axis (rotating shaft) of the outer cylinder 10, or may be configured to rotate indirectly using a mechanism such as a belt or a chain. May be. The direction in which the outer cylinder 10 is rotated is set to a direction in which the water-containing organic matter can be easily stirred and transferred to the rear according to the direction of the stirring blade 11 and the direction of rotation of the inner cylinder 30. In the method for producing a water-containing organic material of this embodiment, the outer cylinder 10 is rotated in the direction of the arrow a shown in FIG. 2, and the tip of the stirring blade 11 is rotated in an inclined direction. Thereby, the water-containing organic substance can be efficiently stirred by the stirring blade 11. The rotational speed of the outer cylinder 10 is appropriately determined so that the above-described filling rate can be maintained.

3.内筒
本実施態様の含水有機物の乾燥装置において、内筒30は、略円筒状のものとなっており、図1に示すように、外筒10の前端部から後端部までを貫通して設けている。内筒30の中心軸は、必ずしも外筒10の中心軸と一致させる必要はないが、本実施態様の含水有機物の乾燥装置では、両方の中心軸(回転軸)を一致させている。内筒30の周壁には、該周壁を内外に連通する複数の通気孔32をスリット状に設けており、熱風発生手段(内筒加熱手段50)によって内筒30内へ送り込まれた熱風が連通孔32を通じて内筒30外へ抜け出るようにしている。これにより、含水有機物をより効率的に乾燥させることが可能となっている。
3. Inner cylinder In the water-containing organic matter drying apparatus of the present embodiment, the inner cylinder 30 has a substantially cylindrical shape, and penetrates from the front end portion to the rear end portion of the outer cylinder 10 as shown in FIG. Provided. The central axis of the inner cylinder 30 is not necessarily coincident with the central axis of the outer cylinder 10, but in the hydrated organic matter drying apparatus of this embodiment, both central axes (rotating axes) are coincident. The peripheral wall of the inner cylinder 30 is provided with a plurality of vent holes 32 that communicate with the inner and outer walls in a slit shape, and the hot air sent into the inner cylinder 30 by the hot air generating means (inner cylinder heating means 50) communicates. Through the hole 32, the outer cylinder 30 is pulled out. Thereby, it becomes possible to dry a water-containing organic substance more efficiently.

また、本実施態様の含水有機物の乾燥装置において、内筒30の外周面には、図1と図2に示すように、撹拌翼31を外向きに設けている。この撹拌翼31によって、押圧ローラ70あるいは外筒10の内周面から内筒30の外周面上へ落下してきた含水有機物を撹拌することが可能になる。本実施態様の含水有機物の乾燥装置においては、図2に示すように、内筒30の中心軸に対して回転対称となるように6本の撹拌翼31を設けている。それぞれの撹拌翼31は、図1に示すように、内筒30の外周面の周方向へ連続的に場所を変えながら内筒30の中心軸方向に延びており、全体としては螺旋状を為している。このため、内筒30をその中心軸回りに回転させると、内筒30と一体的にそれぞれの撹拌翼31も回転するようになっており、撹拌翼11と相俟って含水有機物を後方へと送ることができるようになっている。   Further, in the water-containing organic matter drying apparatus of the present embodiment, a stirring blade 31 is provided outward on the outer peripheral surface of the inner cylinder 30 as shown in FIGS. The agitation blade 31 can agitate the water-containing organic matter that has dropped from the inner surface of the pressing roller 70 or the outer cylinder 10 onto the outer surface of the inner cylinder 30. In the water-containing organic matter drying apparatus of this embodiment, as shown in FIG. 2, six stirring blades 31 are provided so as to be rotationally symmetric with respect to the central axis of the inner cylinder 30. As shown in FIG. 1, each stirring blade 31 extends in the central axis direction of the inner cylinder 30 while continuously changing the position in the circumferential direction of the outer peripheral surface of the inner cylinder 30, and has a spiral shape as a whole. doing. For this reason, when the inner cylinder 30 is rotated about its central axis, each stirring blade 31 is also rotated integrally with the inner cylinder 30, and the water-containing organic matter is moved backward together with the stirring blade 11. Can be sent.

内筒30の外半径(撹拌翼31を除いた外周面の半径。以下、外半径Rとする。)は、特に限定されない。しかし、内筒30の外半径Rを小さくしすぎると、一対の押圧ローラ70によって板状に成形された含水有機物が内筒30上で焼かれる時間が短くなる。一方、内筒30の外半径Rを大きくしすぎると、外筒10の乾燥有効体積Vを大きく確保できなくなるおそれがある。また、含水有機物が移動するスペース(外筒10の内周面と内筒30の外周面との隙間)を確保できなくなり、含水有機物が外筒10内で詰まりやすくなるおそれもある。また、撹拌翼11や撹拌翼31を設けにくくなるおそれもある。このため、外筒10の内半径Rに対する内筒30の外半径Rの比R/Rは、通常、0.03〜0.9、好ましくは、0.5〜0.7、より好ましくは、0.1〜0.5とされる。 Outer radius of the inner cylinder 30 (the radius of the outer circumferential surface excluding the stirring blade 31. Hereinafter, the outer radius R 2.) Is not particularly limited. However, when an outer radius R 2 of the inner tube 30 is too small, the time hydrated organic material is formed into a plate shape by a pair of pressing rollers 70 is burned on the inner cylinder 30 becomes shorter. On the other hand, if the outer radius R 2 of the inner cylinder 30 is too large, there is a possibility that a large effective drying volume V 1 of the outer cylinder 10 cannot be secured. In addition, a space (a gap between the inner peripheral surface of the outer cylinder 10 and the outer peripheral surface of the inner cylinder 30) in which the hydrated organic substance moves cannot be secured, and the hydrated organic substance may be easily clogged in the outer cylinder 10. Moreover, there is a possibility that it is difficult to provide the stirring blade 11 and the stirring blade 31. For this reason, the ratio R 2 / R 1 of the outer radius R 2 of the inner cylinder 30 to the inner radius R 1 of the outer cylinder 10 is usually 0.03 to 0.9, preferably 0.5 to 0.7, More preferably, it is 0.1-0.5.

4.含水有機物供給手段
含水有機物供給手段40は、外筒10の前端部へ含水有機物を供給できるものであれば特に限定されない。本実施態様の含水有機物の乾燥装置において、含水有機物供給手段40は、図1に示すように、含水有機物を投入するためのホッパー41と、ホッパー41から落下してきた含水有機物を後方へ押し出すためのスクリューシリンダ42と、スクリューシリンダ42を収容するための筒状のケーシング43とで構成されたものを採用している。スクリューシリンダ42をその中心軸回りに回転させることによって、含水有機物がケーシング43内を後方へ移動する。スクリューシリンダ43の回転は、スクリューシリンダ回転手段44によって行われる。含水有機物供給手段40におけるスクリューシリンダ42及びケーシング43の後端部は、外筒10内の前端部付近における上部へ挿入されている。このため、含水有機物は、外筒10内における前端部近傍の上部から外筒10内へと供給されるようになっている。
4). Water-containing organic substance supply means The water-containing organic substance supply means 40 is not particularly limited as long as it can supply the water-containing organic substance to the front end portion of the outer cylinder 10. In the water-containing organic matter drying apparatus according to the present embodiment, the water-containing organic matter supplying means 40, as shown in FIG. A screw cylinder 42 and a cylindrical casing 43 for accommodating the screw cylinder 42 are employed. By rotating the screw cylinder 42 about its central axis, the water-containing organic matter moves backward in the casing 43. The screw cylinder 43 is rotated by a screw cylinder rotating means 44. The rear end portions of the screw cylinder 42 and the casing 43 in the water-containing organic substance supply means 40 are inserted into the upper portion in the vicinity of the front end portion in the outer cylinder 10. For this reason, the water-containing organic matter is supplied from the upper part in the vicinity of the front end in the outer cylinder 10 into the outer cylinder 10.

5.内筒加熱手段
内筒加熱手段50は、内筒30を加熱できるものであれば特に限定されない。本実施態様の含水有機物の乾燥装置において、内筒加熱手段50は、内筒30の後方から内筒30内へと熱風を送り込む熱風発生手段となっている。熱風発生手段としては、図示省略のバーナーと、該バーナーで発生した炎を前方へと送る図示省略の送風装置を使用している。本実施態様の含水有機物の乾燥装置において、内筒加熱手段50で発生した熱風は、図1の矢印cで示すように、内筒30内を後方から前方へ通り抜けるようになっている。
5. Inner cylinder heating means The inner cylinder heating means 50 is not particularly limited as long as it can heat the inner cylinder 30. In the water-containing organic matter drying apparatus of this embodiment, the inner cylinder heating means 50 is hot air generating means for sending hot air from the rear of the inner cylinder 30 into the inner cylinder 30. As the hot air generating means, a burner (not shown) and a blower (not shown) for sending the flame generated by the burner forward are used. In the water-containing organic matter drying apparatus of the present embodiment, the hot air generated by the inner cylinder heating means 50 passes through the inner cylinder 30 from the rear to the front, as indicated by an arrow c in FIG.

6.内筒回転手段
内筒回転手段60は、内筒30をその中心軸回りに回転できるものであれば特に限定されない。内筒回転手段60としては、通常、モーターが採用される。内筒回転手段60は、内筒30の中心軸(回転軸)を直接的に回転するように構成してもよいし、ベルトやチェーンなどの機構を用いて間接的に回転するように構成してもよい。内筒30を回転させる向きは、撹拌翼31の向きや外筒10の回転する向きなどに応じて、含水有機物を撹拌しやすく後方へ移送しやすい向きに設定する。本実施態様の含水有機物の乾燥装置において、内筒30は、図2に示す矢印bの向きへ回転させており、外筒10を回転する向きと一致させている。内筒30の回転速度は、上述した充填率などを考慮して適宜決定される。内筒30の回転速度と外筒10の回転速度とを同じにする場合には、内筒30と外筒10とをスポークなどの連結体で接続して一体的に回転するようにすることもできる。このようにすれば、外筒10を回転させれば内筒30も回転するようになるので、内筒回転手段60を別途設ける必要がなくなり、含水有機物の乾燥装置を簡素化してその製造コストなどを削減することが可能になる。
6). Inner cylinder rotating means The inner cylinder rotating means 60 is not particularly limited as long as it can rotate the inner cylinder 30 about its central axis. As the inner cylinder rotating means 60, a motor is usually employed. The inner cylinder rotating means 60 may be configured to directly rotate the central axis (rotating shaft) of the inner cylinder 30, or may be configured to rotate indirectly using a mechanism such as a belt or a chain. May be. The direction in which the inner cylinder 30 is rotated is set to a direction in which the water-containing organic matter is easily stirred and transported backward according to the direction of the stirring blade 31 and the direction of rotation of the outer cylinder 10. In the water-containing organic matter drying apparatus of the present embodiment, the inner cylinder 30 is rotated in the direction of the arrow b shown in FIG. 2, and coincides with the direction of rotation of the outer cylinder 10. The rotational speed of the inner cylinder 30 is appropriately determined in consideration of the above-described filling rate and the like. When the rotation speed of the inner cylinder 30 and the rotation speed of the outer cylinder 10 are the same, the inner cylinder 30 and the outer cylinder 10 may be connected by a connecting body such as a spoke so as to rotate integrally. it can. In this case, if the outer cylinder 10 is rotated, the inner cylinder 30 is also rotated. Therefore, it is not necessary to separately provide the inner cylinder rotating means 60, the water-containing organic matter drying apparatus is simplified, and the manufacturing cost thereof is reduced. Can be reduced.

7.押圧ローラ
押圧ローラ70は、外筒10の前端部付近における上部から供給された含水有機物を両側から押圧して板状に成形できるものであれば特に限定されない。本実施態様の含水有機物の乾燥装置においては、図2に示すように、それぞれの中心軸が互いに平行となるように所定間隔を隔てて平行に配された一対の押圧ローラ70を設けている。それぞれの押圧ローラ70は、中空な円筒状のものとなっており、その内部に熱気を導入することができるようになっており、押圧ローラ70自体も加熱されるようになっている。これにより、含水有機物を押圧ローラ70で板状に成形する際にも、押圧ローラ70で含水有機物を焼いてその表面の水分を蒸発させ、含水有機物をより効率的に乾燥することが可能になる。本実施態様の含水有機物の乾燥装置において、押圧ローラ70の中心軸は、外筒10及び内筒30の中心軸と平行としているが、必ずしも平行にする必要はない。
7). Pressing roller The pressing roller 70 is not particularly limited as long as it can press the water-containing organic material supplied from the upper part in the vicinity of the front end portion of the outer cylinder 10 from both sides to be formed into a plate shape. In the water-containing organic matter drying apparatus of this embodiment, as shown in FIG. 2, a pair of pressing rollers 70 arranged in parallel at a predetermined interval are provided so that the central axes thereof are parallel to each other. Each pressing roller 70 has a hollow cylindrical shape, in which hot air can be introduced, and the pressing roller 70 itself is also heated. Thus, even when the water-containing organic material is formed into a plate shape by the pressing roller 70, the water-containing organic material is baked by the pressure roller 70 to evaporate the water on the surface, and the water-containing organic material can be dried more efficiently. . In the water-containing organic matter drying apparatus according to this embodiment, the central axis of the pressing roller 70 is parallel to the central axes of the outer cylinder 10 and the inner cylinder 30, but is not necessarily parallel.

押圧ローラ70の外半径(外半径Rとする。)は、乾燥対象である含水有機物の種類や特性、あるいは乾燥装置の規模(含水有機物の処理量)などによっても異なり、特に限定されない。しかし、押圧ローラ70の外半径Rを小さくしすぎると、含水有機物供給手段40から外筒10内へ供給された含水有機物が一対の押圧ローラ70の隙間へ導入されにくくなるだけでなく、押圧ローラ70で含水有機物を十分に加熱できなくなり、含水有機物の乾燥効率が低下するおそれがある。というのも、押圧ローラ70の外半径Rが小さいと、押圧ローラ70の回転速度を速くしなければ、外筒10内に供給された含水有機物を滞りなく処理できなくなるが、この場合には、押圧ローラ70の回転周期が短くなって、押圧ローラ70における含水有機物に熱を奪われて温度が低下した部分が1回転して再度含水有機物を押圧するまでにかかる時間も短くなり、当該部分が元の温度まで加熱されなくなるからである。したがって、押圧ローラ70の外半径Rは、外筒10の内周面と内筒30の外周面との間に押圧ローラ70を収容できる範囲でできるだけ大きくすると好ましい。外半径Rなど、押圧ローラ70の寸法的な条件については、後で押圧ローラ70の回転速度について述べる際にも説明する。 The outer radius (referred to as outer radius R 3 ) of the pressing roller 70 is not particularly limited, and varies depending on the type and characteristics of the water-containing organic material to be dried or the scale of the drying device (the amount of water-containing organic material processed). However, too small an outer radius R 3 of the pressing roller 70, not only the water organic matter supplied to the outer cylinder 10 from the water-containing organic substance supply unit 40 is not easily introduced into the gap of the pair of pressing rollers 70, pressing The water-containing organic material cannot be sufficiently heated by the roller 70, and the drying efficiency of the water-containing organic material may be reduced. Because the outer radius R 3 of the pressing roller 70 is small, if a faster rotational speed of the pressing roller 70, but can not be smoothly processed hydrous organic matter supplied to the outer tube 10, in this case , The rotation period of the pressure roller 70 is shortened, and the time taken until the portion of the pressure roller 70 that has been deprived of heat by the water-containing organic material is rotated once to press the water-containing organic material again is shortened. This is because is not heated to the original temperature. Therefore, it is preferable that the outer radius R 3 of the pressing roller 70 be as large as possible within a range in which the pressing roller 70 can be accommodated between the inner peripheral surface of the outer cylinder 10 and the outer peripheral surface of the inner cylinder 30. Such outer radius R 3, for dimensions conditions of the pressure roller 70, also described in describing the rotational speed of the pressing roller 70 later.

一対の押圧ローラ70の間隔(互いの外周面によって形成される隙間の最小値)は、乾燥対象である含水有機物の種類や特性、あるいは乾燥装置の規模(含水有機物の処理量)などによっても異なり、特に限定されない。しかし、一対の押圧ローラ70の間隔を狭くしすぎると、押圧ローラ70の上方に含水有機物が滞留して詰まるおそれがある。このため、一対の押圧ローラ70の間隔は、通常、0.5mm以上とされる。一対の押圧ローラ70の間隔は、1mm以上であると好ましい。一方、一対の押圧ローラ70の間隔を広くしすぎると、押圧ローラ70によって含水有機物を薄い板状に成形できなくなり、含水有機物の乾燥効率が低下するおそれがある。このため、一対の押圧ローラ70の間隔は、通常、10mm以下とされる。一対の押圧ローラ70の間隔は、5mm以下であると好ましく、3mm以下であるとより好ましい。   The distance between the pair of pressing rollers 70 (minimum value of the gap formed by the outer peripheral surfaces) varies depending on the type and characteristics of the water-containing organic matter to be dried, the scale of the drying device (the amount of water-containing organic matter processed), and the like. There is no particular limitation. However, if the distance between the pair of pressing rollers 70 is too narrow, the water-containing organic matter may stay above the pressing rollers 70 and become clogged. For this reason, the space | interval of a pair of press roller 70 shall be 0.5 mm or more normally. The distance between the pair of pressing rollers 70 is preferably 1 mm or more. On the other hand, if the distance between the pair of pressure rollers 70 is too wide, the water-containing organic material cannot be formed into a thin plate by the pressure roller 70, and the drying efficiency of the water-containing organic material may be reduced. For this reason, the distance between the pair of pressing rollers 70 is usually 10 mm or less. The distance between the pair of pressing rollers 70 is preferably 5 mm or less, and more preferably 3 mm or less.

ところで、本実施態様の含水有機物の乾燥装置において、押圧ローラ70は一対のみ設けているが、複数対の押圧ローラ70を設けてもよい。この場合、ある対の押圧ローラ70は、他の対の押圧ローラ70の真下に配すると好ましく、下段に配された一対の押圧ローラ70の間隔を、上段に配された一対の押圧ローラ70の間隔よりも狭くすると好ましい。これにより、含水有機物が塊状で供給された場合であっても、その含水有機物を段階的に板状に成形することが可能になる。このとき、下段に配された一対の押圧ローラ70の回転速度を、上段に配された一対の押圧ローラ70の回転速度よりも速く設定することで、下段に配された押圧ローラ70上に含水有機物が滞留しないようにすることができる。   By the way, in the water-containing organic matter drying apparatus of this embodiment, only one pair of pressing rollers 70 is provided, but a plurality of pairs of pressing rollers 70 may be provided. In this case, it is preferable that a certain pair of pressing rollers 70 is disposed directly below the other pair of pressing rollers 70, and the interval between the pair of pressing rollers 70 disposed in the lower stage is equal to that of the pair of pressing rollers 70 disposed in the upper stage. It is preferable to make it narrower than the interval. Accordingly, even when the water-containing organic material is supplied in a lump shape, the water-containing organic material can be formed into a plate shape step by step. At this time, the rotational speed of the pair of pressing rollers 70 arranged in the lower stage is set to be higher than the rotational speed of the pair of pressing rollers 70 arranged in the upper stage, so that water is contained on the pressing roller 70 arranged in the lower stage. It is possible to prevent the organic matter from staying.

8.押圧ローラ加熱手段
押圧ローラ加熱手段80は、押圧ローラ70を加熱できるものであれば特に限定されない。本実施態様の含水有機物の乾燥装置において、押圧ローラ加熱手段80は、内筒加熱手段50と同様の熱風発生手段を使用しており、図1に示すように、外筒10の前端部を覆うように設けられた前側ダクト100に熱風(図1における矢印d)を送り込むことにより、外筒10内における前端部近傍に配された押圧ローラ70内を前方から後方へ熱風が通り抜けるようにしている。前側ダクト10は、押圧ローラ加熱手段80からの熱風だけでなく、内筒加熱手段50によって内筒30内を後方から前方へ通り抜けた熱風を折り返して外筒10内へ導入する機能をも有するものとなっている。押圧ローラ加熱手段80から送られて押圧ローラ70を後方へ通り抜けた熱風、及び内筒加熱手段50から送られて外筒10内へ導入された熱風は、図1の矢印eに示すように、外筒10内を前方から後方へ通り抜け、図1の矢印fに示すように、外筒10の後端部を覆うように設けられた後側ダクト110を通り、外気へ放出、又は図示省略の乾燥排ガス処理装置へと送られる。
8). Pressing roller heating means The pressing roller heating means 80 is not particularly limited as long as it can heat the pressing roller 70. In the water-containing organic matter drying apparatus of this embodiment, the pressing roller heating means 80 uses hot air generating means similar to the inner cylinder heating means 50 and covers the front end of the outer cylinder 10 as shown in FIG. By sending hot air (arrow d in FIG. 1) into the front duct 100 provided in this manner, the hot air passes from the front to the back through the pressing roller 70 disposed in the vicinity of the front end portion in the outer cylinder 10. . The front duct 10 has not only hot air from the pressing roller heating means 80 but also a function of folding back hot air that has passed through the inner cylinder 30 from the rear to the front by the inner cylinder heating means 50 and introducing it into the outer cylinder 10. It has become. The hot air sent from the pressure roller heating means 80 and passed through the pressure roller 70 rearward, and the hot air sent from the inner cylinder heating means 50 and introduced into the outer cylinder 10 are as shown by an arrow e in FIG. As shown by an arrow f in FIG. 1, it passes through the outer cylinder 10 from the front to the rear, passes through a rear duct 110 provided so as to cover the rear end portion of the outer cylinder 10, and is discharged to the outside air or not shown. It is sent to the dry exhaust gas treatment device.

9.押圧ローラ回転手段
押圧ローラ回転手段90は、押圧ローラ70をその中心軸回りに回転できるものであれば特に限定されない。押圧ローラ回転手段90としては、通常、モーターが採用される。押圧ローラ回転手段90は、押圧ローラ70の中心軸(回転軸)を直接的に回転するように構成してもよいし、ベルトやチェーンなどの機構を用いて間接的に回転するように構成してもよい。押圧ローラ70は、含水有機物供給手段40から外筒10内へ供給された含水有機物を板状に成形できるように、図2の矢印gに示すように、対となる押圧ローラ70側で上方から下方へと回転する向きに回転される。押圧ローラ70の回転速度は、特に限定されないが、押圧ローラ70の回転速度をX[rpm]、含水有機物の処理量をV[m/h]、押圧ローラ70の間隔をT[mm]、押圧ローラ70の有効長さ(押圧ローラ70の軸方向全体長のうち、含水有機物を成形するのに作用する区間の長さ。)をL[cm]、押圧ローラ70の外半径をR[cm]とした場合に、下記式1で表わされる値に設定すると好ましい。
X=V×10÷(6×L×R×T) ・・・式1
これにより、含水有機物供給手段40から供給されてくる含水有機物を滞りなく処理することが可能になる。
9. Pressing roller rotating means The pressing roller rotating means 90 is not particularly limited as long as it can rotate the pressing roller 70 around its central axis. As the pressing roller rotating means 90, a motor is usually employed. The pressing roller rotating means 90 may be configured to directly rotate the central axis (rotating shaft) of the pressing roller 70, or may be configured to rotate indirectly using a mechanism such as a belt or a chain. May be. As shown by the arrow g in FIG. 2, the pressing roller 70 is formed from above on the paired pressing roller 70 side so that the water-containing organic material supplied from the water-containing organic material supplying means 40 into the outer cylinder 10 can be formed into a plate shape. It is rotated in the direction of rotating downward. The rotational speed of the pressure roller 70 is not particularly limited, but the rotational speed of the pressure roller 70 is X [rpm], the treatment amount of the water-containing organic matter is V [m 3 / h], and the interval between the pressure rollers 70 is T [mm]. The effective length of the pressing roller 70 (the length of the section acting to form the water-containing organic matter in the entire axial length of the pressing roller 70) is L [cm], and the outer radius of the pressing roller 70 is R 3 [ cm], it is preferable to set the value represented by the following formula 1.
X = V × 10 6 ÷ (6 × L × R 3 × T) Equation 1
Thereby, it becomes possible to process the water-containing organic substance supplied from the water-containing organic substance supply means 40 without delay.

10.含水有機物の乾燥方法
本実施態様の含水有機物の乾燥装置を使用した含水有機物の乾燥方法について説明する。含水有機物は、図1に示すように、含水有機物供給手段40におけるホッパー41に投入する。ホッパー41に投入された含水有機物は、ホッパー41内を下方へ移動し、その下方のケーシング43の前側へ導入される。ケーシング43内へ導入された含水有機物は、スクリューシリンダ42によって後方へ押し出され、外筒10内の前端部近傍の上部から外筒10内へ供給される。
10. Method for Drying Water-Containing Organic Material A method for drying a water-containing organic material using the water-containing organic material drying apparatus of this embodiment will be described. As shown in FIG. 1, the water-containing organic substance is put into a hopper 41 in the water-containing organic substance supply means 40. The water-containing organic substance thrown into the hopper 41 moves downward in the hopper 41 and is introduced to the front side of the casing 43 below the hopper 41. The water-containing organic substance introduced into the casing 43 is pushed backward by the screw cylinder 42 and supplied into the outer cylinder 10 from the upper part in the vicinity of the front end portion in the outer cylinder 10.

外筒10内へ供給された含水有機物は、その両側を一対の押圧ローラ70によって押圧されることにより板状に成形され、内筒10の外周面上へと落下する。このとき、含水有機物は、押圧ローラ70によって焼かれるため、それに含有される水分の一部が蒸発する。内筒10上へ落下した含水有機物は、加熱された内筒30によって焼かれながら内筒30とともに回転する。このとき、含水有機物は、それに含まれる水分の大部分が蒸発し、粒状となる。内筒30に貼りついた状態の含水有機物は、内筒30が半周程度回転すると、重力により、外筒10の上向きの内周面(外筒10の内底面)へ落下する。   The water-containing organic substance supplied into the outer cylinder 10 is formed into a plate shape by pressing both sides thereof by a pair of pressing rollers 70 and falls onto the outer peripheral surface of the inner cylinder 10. At this time, since the water-containing organic material is baked by the pressing roller 70, a part of the water contained therein evaporates. The water-containing organic matter that has dropped onto the inner cylinder 10 rotates with the inner cylinder 30 while being baked by the heated inner cylinder 30. At this time, most of the moisture contained in the water-containing organic material evaporates and becomes granular. The water-containing organic matter adhered to the inner cylinder 30 falls to the upward inner peripheral surface of the outer cylinder 10 (the inner bottom surface of the outer cylinder 10) by gravity when the inner cylinder 30 rotates about a half circumference.

外筒10の内底面へ落下した含水有機物は、外筒10の回転によって外筒内10を上方へかき揚げられ、再度、内筒10上へ落下する。このとき、含水有機物は、撹拌翼11、撹拌翼31、あるいは外筒10内を前方から後方へ通り抜ける熱風によって外筒10内を後方へ移動していく。含水有機物は、外筒10内を後方へ移動するにつれて、外筒10内を通り抜ける熱風や内筒30の熱などによってさらに乾燥していき、細粒状あるいは粉状となる。外筒10の後端部に達した含水有機物は、完全に乾燥した状態となっている。乾燥した含水有機物は、図1に示す矢印hのように、後側ダクト110の下部に設けられた含水有機物送出管120内へ落下し、乾燥装置の外部へと取り出される。取り出された含水有機物(乾燥物)は、肥料などの原料として再利用することも可能である。   The water-containing organic matter that has fallen to the inner bottom surface of the outer cylinder 10 is scraped upward in the outer cylinder 10 by the rotation of the outer cylinder 10 and falls again onto the inner cylinder 10. At this time, the water-containing organic matter moves backward in the outer cylinder 10 by hot air passing from the front to the rear in the stirring blade 11, the stirring blade 31, or the outer cylinder 10. As the water-containing organic substance moves rearward in the outer cylinder 10, it is further dried by hot air passing through the outer cylinder 10, heat of the inner cylinder 30, etc., and becomes fine or powdery. The water-containing organic matter that has reached the rear end of the outer cylinder 10 is in a completely dry state. The dried hydrated organic matter falls into the hydrated organic matter delivery pipe 120 provided at the lower portion of the rear duct 110 as indicated by an arrow h shown in FIG. 1, and is taken out of the drying apparatus. The extracted water-containing organic matter (dry matter) can be reused as a raw material for fertilizers and the like.

11.用途
本発明の含水有機物の乾燥装置は、その用途を限定されるものではなく、各種の含水有機物を乾燥するのに用いることができる。本発明の含水有機物の乾燥装置で好適に乾燥できる含水有機物としては、汚泥や生ゴミや畜産廃棄物などが例示される。本発明の含水有機物の乾燥装置を用いることにより、これらの含水有機物を有効な資源(例えば肥料や燃料など)として容易に再利用することも可能である。
11. Use The use of the water-containing organic matter drying apparatus of the present invention is not limited, and can be used to dry various kinds of water-containing organic matter. Examples of the water-containing organic material that can be suitably dried by the water-containing organic material drying apparatus of the present invention include sludge, raw garbage, and livestock waste. By using the water-containing organic matter drying apparatus of the present invention, these water-containing organic materials can be easily reused as effective resources (for example, fertilizer and fuel).

10 外筒
11 撹拌翼
20 外筒回転手段
30 内筒
31 撹拌翼
32 連通孔
40 含水有機物供給手段
41 ホッパー
42 スクリューシリンダ
43 ケーシング
44 スクリューシリンダ回転手段
50 内筒加熱手段
60 内筒回転手段
70 押圧ローラ
80 押圧ローラ加熱手段
90 押圧ローラ回転手段
100 前側ダクト
110 後側ダクト
120 含水有機物送出管

DESCRIPTION OF SYMBOLS 10 Outer cylinder 11 Stirring blade 20 Outer cylinder rotating means 30 Inner cylinder 31 Stirring blade 32 Communication hole 40 Hydrous organic substance supply means 41 Hopper 42 Screw cylinder 43 Casing 44 Screw cylinder rotating means 50 Inner cylinder heating means 60 Inner cylinder rotating means 70 Press roller 80 Pressure roller heating means 90 Pressure roller rotation means 100 Front duct 110 Rear duct 120 Hydrous organic matter delivery pipe

Claims (5)

その中心軸が前後方向に向けられ、その中心軸回りに回転する外筒と、
外筒内に収容されて外筒の中心軸に沿って配され、その中心軸回りに回転する内筒と、
外筒の前方に設けられた供給部から外筒内へと含水有機物を供給し、含水有機物を内筒の外周面上へ落下させる含水有機物供給手段と、
内筒を加熱する内筒加熱手段と
筒内へ供給されて内筒の外周面上へ落下する前の含水有機物を両側から押圧する少なくとも一対の押圧ローラと、
それぞれの押圧ローラをその中心軸周りに回転させる押圧ローラ回転手段と、
を備え、
押圧ローラで板状に成形された含水有機物を撹拌するための第一の撹拌翼が、内筒の外周面から外向きに設けられるとともに、
内筒の外周面から落下してきた含水有機物を外筒内の上部へとかき揚げるための第二の撹拌翼が、外筒の内周面から内向きに設けられ、
一対の押圧ローラが、含水有機物供給手段の供給部の真下であって、内筒の真上となる箇所に配され、
含水有機物供給手段の供給部から外筒内へ供給された含水有機物を押圧ローラで板状に成形してから内筒の外周面上へと落下させ、該含水有機物を内筒で熱しながら外筒の後方へ移送することができるようにしたことを特徴とする含水有機物の乾燥装置。
An outer cylinder whose center axis is directed in the front-rear direction and rotates about the center axis ;
An inner cylinder housed in the outer cylinder and arranged along the central axis of the outer cylinder, and rotating around the central axis ;
Water-containing organic matter supplying means for supplying water-containing organic matter into the outer cylinder from a supply section provided in front of the outer cylinder, and dropping the water-containing organic matter onto the outer peripheral surface of the inner cylinder;
An inner cylinder heating means for heating the inner cylinder ;
At least a pair of pressing rollers that press the water-containing organic matter from both sides before being supplied into the outer cylinder and falling onto the outer peripheral surface of the inner cylinder;
A pressing roller rotating means for rotating each pressing roller around its central axis;
With
The first stirring blade for stirring the water-containing organic material formed into a plate shape by the pressing roller is provided outward from the outer peripheral surface of the inner cylinder,
A second agitating blade is provided inward from the inner peripheral surface of the outer cylinder, for lifting the water-containing organic matter falling from the outer peripheral surface of the inner cylinder to the upper part in the outer cylinder;
A pair of pressing rollers is disposed immediately below the supply portion of the water-containing organic substance supply means, and directly above the inner cylinder,
The hydrous organic substance supplied from the supply part of the hydrous organic substance supply means into the outer cylinder is formed into a plate shape by a pressing roller, then dropped onto the outer peripheral surface of the inner cylinder, and the outer cylinder is heated while the hydrous organic substance is heated by the inner cylinder A device for drying a water-containing organic material, characterized in that it can be transported to the rear of the water.
内筒加熱手段が、内筒の後方から内筒内へと熱風を送り込む熱風発生手段である請求項1記載の含水有機物の乾燥装置。   The apparatus for drying a water-containing organic substance according to claim 1, wherein the inner cylinder heating means is hot air generating means for sending hot air from the rear of the inner cylinder into the inner cylinder. 内筒の周壁に該周壁を内外に連通する複数の通気孔を設け、熱風発生手段によって内筒内へ送り込まれた熱風が前記連通孔を通じて内筒外へ抜け出るようにした請求項2記載の含水有機物の乾燥装置。   The water content according to claim 2, wherein a plurality of ventilation holes are provided in the peripheral wall of the inner cylinder so as to communicate the inner wall with the outer wall, and the hot air sent into the inner cylinder by the hot air generating means escapes outside the inner cylinder through the communication hole. Organic matter drying equipment. 押圧ローラを加熱するための押圧ローラ加熱手段を内筒加熱手段とは独立して設けた請求項1〜3いずれか記載の含水有機物の乾燥装置。   The water-containing organic matter drying apparatus according to any one of claims 1 to 3, wherein a pressing roller heating means for heating the pressing roller is provided independently of the inner cylinder heating means. 一対の押圧ローラが複数組設けられ、一の組の一対の押圧ローラが他の組の一対の押圧ローラの真下に配され、下段に配された一対の押圧ローラの間隔が、上段に配された一対の押圧ローラの間隔よりも狭くされた請求項1〜4いずれか記載の含水有機物の乾燥装置。A plurality of pairs of pressure rollers are provided, one pair of pressure rollers is disposed directly below the other pair of pressure rollers, and the distance between the pair of pressure rollers disposed on the lower stage is disposed on the upper stage. The water-containing organic matter drying device according to any one of claims 1 to 4, wherein the drying device is narrower than a distance between the pair of pressing rollers.
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