JP4505472B2 - Sludge drying equipment - Google Patents

Sludge drying equipment Download PDF

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JP4505472B2
JP4505472B2 JP2007008007A JP2007008007A JP4505472B2 JP 4505472 B2 JP4505472 B2 JP 4505472B2 JP 2007008007 A JP2007008007 A JP 2007008007A JP 2007008007 A JP2007008007 A JP 2007008007A JP 4505472 B2 JP4505472 B2 JP 4505472B2
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cylinder
drying
screw conveyor
screw
drying chamber
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JP2008173551A (en
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正一 内村
俊太郎 伊勢
章生 小串
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ISE FOODS Inc
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ISE FOODS Inc
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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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

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  • Treatment Of Sludge (AREA)
  • Drying Of Solid Materials (AREA)

Description

本発明は、被乾燥物を効果的に加熱し効率よく乾燥させることができる乾燥装置に関する。   The present invention relates to a drying apparatus capable of effectively heating an object to be dried and drying it efficiently.

例えば、汚水処理場の汚泥、鶏糞、おから等のような食品廃棄物、生ゴミ等は、含水率が数十パーセントから高いものでは90%程度のものもある。従って、これらのものが、最終的に焼却、埋立、コンポスト原料としての利用等様々な処理をされる際には、それに先立ち含水率を低下(乾燥)させる必要がある。   For example, sludge, sewage waste, food waste such as chicken excrement, okara etc., raw garbage, etc. in a sewage treatment plant may have a water content of several tens to about 90%. Therefore, when these materials are finally subjected to various treatments such as incineration, landfill, and utilization as compost raw materials, it is necessary to lower (dry) the moisture content prior to that.

このような含水率を低下(乾燥)させる必要があるもの(以下、「被乾燥物」という。)を、乾燥させる方法は様々な方法が知られている。例えば、天日に干したり、風乾させたりといったことも行われてきたが、効率的な乾燥を行うことができないことから、多くの乾燥装置が発明考案され用いられてきた。   Various methods are known for drying such a water content that needs to be reduced (dried) (hereinafter referred to as “substance to be dried”). For example, although it has been carried out such as drying in the sun or air-drying, many drying apparatuses have been invented and used since efficient drying cannot be performed.

下記特許文献1は発明者等が、生ゴミ分別機で分別されると共に、破砕された生ゴミを乾燥するための生ゴミ乾燥機として発明したものである。
特許第3595201号
The following Patent Document 1 was invented by the inventors as a garbage dryer for separating garbage with a garbage separator and drying the crushed garbage.
Japanese Patent No. 3595201

図4に示すように、乾燥室2は、薄い方形体で内部に多段(図面では8段)に横方向に延長した筒体6が水平に設けられ、筒体6は端部が上または下の筒体6の端部に交互に連結部6Aにより連通されて一本に形成されている。   As shown in FIG. 4, the drying chamber 2 is a thin rectangular body that is internally provided with a horizontally extending cylinder 6 extending in multiple stages (eight stages in the drawing), and the end of the cylinder 6 is at the top or bottom. The end portions of the cylindrical body 6 are alternately connected to each other by the connecting portions 6A and formed into one.

そして、最上部の筒体6に乾燥室2外に通じる生ゴミ投入口7が設けられ、また最下部の筒体6に乾燥室2外に通じる生ゴミ排出口8が設けられている。   The uppermost cylinder 6 is provided with a garbage input port 7 that leads to the outside of the drying chamber 2, and the lowermost cylinder 6 is provided with a garbage outlet 8 that leads to the outside of the drying chamber 2.

図示は省略するが、生ゴミ投入口7の上方に生ゴミ投入管口より投入された生ゴミを筒体6に押し込むための押圧シリンダーが設けられている。また、生ゴミ排出口8の下方に搬送用のベルトコンベアが設けられている。   Although not shown in the drawing, a pressing cylinder for pushing the garbage introduced from the garbage input pipe port into the cylindrical body 6 is provided above the garbage input port 7. A conveyor belt for conveyance is provided below the garbage discharge port 8.

また、各段の筒体6内に夫々スクリューコンベア12が内蔵されている。各段のスクリューコンベア12は往路と復路が上下に交互になるよう配設されている。各スクリューコンベア12はモーター13の回転がチェーン14とスプロケット15による連動機構により伝達され、同一回転する。   Moreover, the screw conveyor 12 is each incorporated in the cylinder 6 of each step. The screw conveyors 12 at each stage are arranged so that the forward path and the return path are alternately up and down. Each screw conveyor 12 is rotated by the rotation of the motor 13 by the interlocking mechanism formed by the chain 14 and the sprocket 15.

また、乾燥室2内の筒体6の周囲に耐熱性材料のガラスまたはセラミックス等の細粒体16が充填されている。   In addition, fine particles 16 such as glass or ceramics of a heat resistant material are filled around the cylinder 6 in the drying chamber 2.

また、筒体6の連結部6Aに筒体6内で発生した蒸気が送出される蒸気送出口17が設けられ、この蒸気送出口17に蒸気送出管の一端が連結される。   Further, a steam outlet 17 through which steam generated in the cylinder 6 is sent out is provided in the connecting portion 6 </ b> A of the cylinder 6, and one end of the steam delivery pipe is connected to the steam outlet 17.

筒体6内の生ゴミは生ゴミ投入口7より押し込まれ、スクリューコンベア12により圧搾されながら搬送されるので、生ゴミ中に含まれる水分は筒体6内で分離される。そして、分離された水分は筒体6が受ける熱気で蒸気と化し、筒体6から送給手段により一次燃焼室に送り込まれ、一次燃焼室で気化される。   Since the garbage in the cylinder 6 is pushed in from the garbage input port 7 and is transported while being compressed by the screw conveyor 12, the moisture contained in the garbage is separated in the cylinder 6. The separated moisture is converted into steam by the hot air received by the cylinder 6, and is sent from the cylinder 6 to the primary combustion chamber by the feeding means, and is vaporized in the primary combustion chamber.

また、筒体6は上下方向に多段に設けられ、端部が交互に上下に連通されて一本に形成されているため、生ゴミは長距離搬送され、乾燥時間も長くなり、小さな乾燥室であっても十分な乾燥を受ける。   In addition, since the cylindrical body 6 is provided in multiple stages in the vertical direction and the ends are alternately communicated with each other in the vertical direction, the garbage is transported for a long distance, the drying time is increased, and a small drying chamber is formed. Even get enough drying.

また、筒体6は直接火炎が当たらず、間接熱によること及び筒体6の周囲を細粒体16で充填してあることにより、筒体6の熱による変形が防止されると共に、細粒体16により保温性を有し、燃料の節約になる。   In addition, the cylindrical body 6 is not directly exposed to flames, and due to the indirect heat and the periphery of the cylindrical body 6 is filled with the fine particles 16, deformation of the cylindrical body 6 due to heat is prevented, and the fine particles The body 16 has heat retention and saves fuel.

前記特許文献1は生ゴミ乾燥機であり、これが粘度が高い被乾燥物や固体を多く含む被乾燥物(一例としては、汚泥や食品廃棄物等)等では、スクリューコンベア12のスクリューに被乾燥物が付着したりして、非常に乾燥効率が悪いものとなる。   The above-mentioned Patent Document 1 is a garbage dryer, which is to be dried on the screw of the screw conveyor 12 for a high-viscosity to-be-dried object or a to-be-dried object that contains a lot of solids (for example, sludge or food waste). A thing adheres and it becomes a thing with very bad drying efficiency.

また、筒体6は上下方向に多段に設けられ、端部が交互に上下に連通されて一本に形成されているため、長距離搬送され、乾燥時間も長くなり、小さな乾燥室であっても十分な乾燥を受けることができるが、その分バーナー燃焼のための燃料費が高騰する。   In addition, since the cylindrical body 6 is provided in multiple stages in the vertical direction and the end portions are alternately communicated with each other in the vertical direction, the cylindrical body 6 is transported over a long distance, and the drying time is increased. However, the fuel cost for burner combustion rises accordingly.

本発明の目的は前記従来例の不都合を解消し、粘度が高い被乾燥物や固体を多く含む被乾燥物(一例としては、汚泥や鶏糞や食品廃棄物等)等であっても被乾燥物をうまく乾燥させることができ、しかも、燃料費も節約できる汚泥等の乾燥装置を提供することにある。   The object of the present invention is to overcome the disadvantages of the above-mentioned conventional example, and to be dried even if it is a dried object having a high viscosity or a dried substance containing a lot of solids (for example, sludge, chicken manure, food waste, etc.) It is an object of the present invention to provide a drying apparatus such as sludge that can be dried well and can save fuel costs.

前記目的を達成するため請求項1記載の本発明は、乾燥室内に、上下方向に多段に横方向に延長する内部にスクリューコンベアが内蔵された筒体が設けられると共に、各筒体は端部が上または下の筒体の端部と交互に連通されて一本に形成され、前記スクリューコンベアは往路と復路が上下に交互になるよう配設され、端部の筒体に乾燥室外に通じる投入口が設けられると共に、他の端部の筒体に乾燥室外に通じる排出口が設けられる乾燥装置において、スクリューコンベアのスクリュー軸は中空とし、一端はホウ金製のブッシュを介して軸受けで軸支され、軸受けの外周にはグリース注入用の給油溝を形成し、このスクリューコンベアのスクリュー軸の端部の軸受けを貫通してスクリュー軸内に電気ヒーターを配設したことを要旨とするものである。 In order to achieve the above-mentioned object, the present invention according to claim 1 is provided with a cylindrical body in which a screw conveyor is incorporated in a drying chamber and is extended in the horizontal direction in multiple stages in the vertical direction, and each cylindrical body has an end portion. Are connected to the end of the upper or lower cylinder alternately and formed into one, and the screw conveyor is arranged so that the forward path and the return path are alternated vertically, and the end cylinder communicates with the outside of the drying chamber. In the drying apparatus in which the inlet is provided and the outlet at the other end is provided with a discharge port that leads to the outside of the drying chamber, the screw shaft of the screw conveyor is hollow, and one end is supported by a bearing through a bushing made of gold. It is supported also on the outer periphery of the bearing to form a oil supply groove for grease, and summarized in that an electric heater is disposed inside the screw shaft through the bearing end of the screw shaft of the screw conveyor It is.

請求項1記載の本発明によれば、スクリューコンベアのスクリュー軸内に電気ヒーターを配設したことにより、バーナーでの加熱と合わせてスクリューコンベアの内外から加熱することができ、これにより、迅速な乾燥、炭化が行え、粘度が高い被乾燥物や固体を多く含む被乾燥物(一例としては、汚泥や食品廃棄物等)等であっても被乾燥物をうまく乾燥させることができる。   According to the first aspect of the present invention, since the electric heater is provided in the screw shaft of the screw conveyor, it can be heated from the inside and outside of the screw conveyor together with the heating by the burner. Even if it is a thing to be dried and carbonized and has a high viscosity or a substance to be dried containing a large amount of solids (for example, sludge or food waste), the substance to be dried can be successfully dried.

また、スクリューコンベアのスクリュー軸の内側からの加熱を行うことにより、筒体外側からの加熱量をその分減少することができ、燃料費を削減することができる。   Further, by heating from the inside of the screw shaft of the screw conveyor, the amount of heating from the outside of the cylindrical body can be reduced correspondingly, and the fuel cost can be reduced.

さらに、電気ヒーターは、スクリューコンベアのスクリュー軸の端部の軸受けを貫通して、スクリュー軸内に配設することで、スクリュー軸が回転してもこの電気ヒーターは回転せずにすみ、また、スクリュー軸が熱により膨張してもその影響を受けないですむ。 Furthermore, the electric heater penetrates the bearing at the end of the screw shaft of the screw conveyor and is arranged in the screw shaft, so that the electric heater does not rotate even if the screw shaft rotates, Even if the screw shaft expands due to heat, it is not affected.

以上述べたように本発明の汚泥等の乾燥装置は、粘度が高い被乾燥物や固体を多く含む被乾燥物等であっても被乾燥物を効率良く乾燥させることができ、しかも、燃料費も節約できるものである。   As described above, the drying apparatus such as sludge according to the present invention can efficiently dry a to-be-dried object even if the object to be dried has a high viscosity or a to-be-dried substance containing a large amount of solids. Can also save money.

以下、図面について本発明の実施の形態を詳細に説明する。図1は本発明の汚泥等の乾燥装置の1実施形態を示す要部の縦断側面図で、図中12はスクリューコンベアである。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. FIG. 1 is a longitudinal side view of a main part showing one embodiment of a drying apparatus for sludge and the like of the present invention. In the figure, 12 is a screw conveyor.

本発明も前記図4で示す従来例と同じく、スクリューコンベア12は筒体6に内蔵されたものであり、図2に示すように、バーナー4aで加熱する乾燥室2内に、上下方向に多段に横方向に延長するように設けられる。   In the present invention, as in the conventional example shown in FIG. 4, the screw conveyor 12 is built in the cylindrical body 6. As shown in FIG. It is provided to extend in the lateral direction.

前記各筒体6は端部が上または下の筒体6の端部と交互に連通されて一本に形成され、前記スクリューコンベア12は往路と復路が上下に交互になるよう配設される。   Each cylindrical body 6 is formed in one piece with the ends thereof alternately communicating with the ends of the upper or lower cylindrical body 6, and the screw conveyor 12 is arranged so that the forward path and the backward path are alternated up and down. .

本実施形態では、最上部の筒体6に乾燥室2外に通じる投入口18が設けられ、また最下部の筒体6に乾燥室2外に通じる排出口19が設けられている。   In the present embodiment, the uppermost cylinder 6 is provided with an inlet 18 that communicates with the outside of the drying chamber 2, and the lowermost cylinder 6 is provided with an outlet 19 that communicates with the outside of the drying chamber 2.

図2中、20はメインホッパー、21はサブホッパーで、メインホッパー20には取出しスクリューコンベア22を設けてこれでサブホッパー21に搬送し、サブホッパー21には投入スクリューコンベア23を設けてこれで投入口18に搬送する。   In FIG. 2, 20 is a main hopper, 21 is a sub hopper, the main hopper 20 is provided with a take-out screw conveyor 22 and conveyed to the sub hopper 21, and the sub hopper 21 is provided with a loading screw conveyor 23. It is conveyed to the inlet 18.

また、排出口19には排出スクリューコンベア24を置いて乾燥物αを排出する。図中3はスクリューコンベア駆動用のモーターである。   A discharge screw conveyor 24 is placed at the discharge port 19 to discharge the dry matter α. In the figure, 3 is a motor for driving the screw conveyor.

図中1は脱臭処理室で、これは乾燥室2と二室接続ダクト5で接続され、バーナー4bで乾燥室2の燃焼ガスを加熱して、ダイオキシンを分解する(800℃)。   In the figure, reference numeral 1 denotes a deodorizing treatment chamber, which is connected to the drying chamber 2 by a two-chamber connecting duct 5, and the combustion gas in the drying chamber 2 is heated by a burner 4b to decompose dioxins (800 ° C.).

乾燥室2も脱臭処理室1も負圧(ブロアー吸引)をかけるが、25は吸引用のブロアーである。   Both the drying chamber 2 and the deodorizing treatment chamber 1 apply negative pressure (blower suction), and 25 is a suction blower.

なお、前記実施形態では、最上部の筒体6に乾燥室2外に通じる投入口18が設けられ、また最下部の筒体6に乾燥室2外に通じる排出口19が設けられて上部から投入したものを下部から取出すようにしたが、逆に最上部の筒体6に乾燥室2外に通じる排出口を設け、最下部の筒体6に乾燥室2外に通じる投入口を設けて下から上へと搬送して取出すようにしてもよい。   In the above-described embodiment, the uppermost cylinder 6 is provided with an inlet 18 that communicates with the outside of the drying chamber 2, and the lowermost cylinder 6 is provided with an outlet 19 that communicates with the outside of the drying chamber 2. What was thrown in was taken out from the lower part, but on the contrary, the uppermost cylinder 6 was provided with a discharge port leading to the outside of the drying chamber 2, and the lowermost cylinder 6 was provided with an inlet opening leading to the outside of the drying chamber 2. It may be conveyed from the bottom to the top and taken out.

本発明は、前記上下方向に多段に横方向に延長する筒体6の内部に設けるスクリューコンベア12のスクリュー軸12aを中空とし、このスクリュー軸12a内に電気ヒーター26を配設した。12bはスクリュー羽根である。一例として電気ヒーター26は、電源AC200V、容量4.2kW[1.4kW×3本(Δ結線)]、径φ8のSUS304のシースに内蔵したニクロム線ヒーターによる。   In the present invention, the screw shaft 12a of the screw conveyor 12 provided inside the cylindrical body 6 extending in the horizontal direction in multiple stages in the vertical direction is hollow, and the electric heater 26 is disposed in the screw shaft 12a. 12b is a screw blade. As an example, the electric heater 26 is a nichrome wire heater built in a sheath of SUS304 having a power source of AC 200 V, a capacity of 4.2 kW [1.4 kW × 3 (Δ connection)], and a diameter φ8.

スクリュー軸12aは図示は省略するが、一端はモーター3側に連結し、他端は図1に示すようにホウ金製のブッシュ27を介して軸受け28で軸支される。軸受け28の外周にはグリース注入用の給油溝29を形成した。   Although the screw shaft 12a is not shown, one end is connected to the motor 3 side, and the other end is pivotally supported by a bearing 28 via a bush 27 made of gold wire as shown in FIG. An oil supply groove 29 for injecting grease was formed on the outer periphery of the bearing 28.

前記電気ヒーター26は図3に示すように長尺なものであり、前記軸受け28を貫通して、スクリュー軸12a内に配設する。   The electric heater 26 is long as shown in FIG. 3, and is disposed in the screw shaft 12a through the bearing 28.

このようにして、汚泥は投入口18より筒体6内に押し込まれ、スクリューコンベア12により搬送され、乾燥室2内で、筒体6の外側からバーナー4aで加熱(約550℃)される。筒体6には孔6bを形成して外側からの加熱を促進させてもよい。   In this way, the sludge is pushed into the cylinder 6 from the charging port 18, conveyed by the screw conveyor 12, and heated (about 550 ° C.) by the burner 4 a from the outside of the cylinder 6 in the drying chamber 2. The cylinder 6 may be formed with a hole 6b to promote heating from the outside.

また、スクリューコンベア12の内側からもスクリュー軸12a内に電気ヒーター26で加熱され(約350℃)、乾燥が行われる。   In addition, the screw shaft 12a is also heated from the inside of the screw conveyor 12 by the electric heater 26 (about 350 ° C.) and dried.

汚泥中から出る水分や排ガスは二室接続ダクト5で脱臭処理室1に送られ、さらに加熱され、ダイオキシン等が除去される。   Moisture and exhaust gas coming out of the sludge is sent to the deodorizing treatment chamber 1 through the two-chamber connecting duct 5 and further heated to remove dioxins and the like.

このように、筒体6は上下方向に多段に設けられ、端部が交互に上下に連通されて一本に形成されているため、汚泥は長距離搬送され、乾燥時間も長くなり、小さな乾燥室であっても十分な乾燥を受ける。   As described above, the cylindrical body 6 is provided in multiple stages in the vertical direction, and the end portions are alternately communicated with each other in the vertical direction, so that the sludge is transported for a long distance, the drying time is increased, and the small drying is performed. Even in a room, it is thoroughly dried.

また、スクリューコンベア12のスクリュー軸12aが回転しても、電気ヒーター26は回転せず、スクリュー軸12aが熱で膨張しても、この電気ヒーター26には影響を与えない。   Moreover, even if the screw shaft 12a of the screw conveyor 12 rotates, the electric heater 26 does not rotate, and even if the screw shaft 12a expands due to heat, the electric heater 26 is not affected.

本発明の汚泥等の乾燥装置の1実施形態を示す要部の縦断側面図である。It is a vertical side view of the principal part which shows one Embodiment of drying apparatuses, such as sludge of this invention. 汚泥等の乾燥装置の全体の説明図である。It is explanatory drawing of the whole drying apparatuses, such as sludge. 電気ヒーターの側面図である。It is a side view of an electric heater. 従来例である生ゴミ乾燥機の一実施の形態を示す部分縦断側面図である。It is a partial vertical side view which shows one Embodiment of the garbage dryer which is a prior art example.

1…脱臭処理室 2…乾燥室
3…モーター 4a、4b…バーナー
5…二室接続ダクト 6…筒体
6A…連結部 6b…孔
7…生ゴミ投入口 8…生ゴミ排出口
12…スクリューコンベア 12a…スクリュー軸
12b…スクリュー羽根 13…モーター
14…チェーン 15…スプロケット
16…細粒体 17…蒸気送出口
18…投入口 19…排出口
20…メインホッパー 21…サブホッパー
22…取出しスクリューコンベア 23…投入スクリューコンベア
24…排出スクリューコンベア 25…ブロアー
26…電気ヒーター 27…ブッシュ
28…軸受け 29…給油溝
DESCRIPTION OF SYMBOLS 1 ... Deodorizing treatment chamber 2 ... Drying chamber 3 ... Motor 4a, 4b ... Burner 5 ... Two-chamber connection duct 6 ... Cylindrical body 6A ... Connection part 6b ... Hole 7 ... Garbage input port 8 ... Garbage discharge port 12 ... Screw conveyor 12a ... Screw shaft 12b ... Screw blade 13 ... Motor 14 ... Chain 15 ... Sprocket 16 ... Fine granule 17 ... Steam outlet 18 ... Input port 19 ... Discharge port 20 ... Main hopper 21 ... Sub hopper 22 ... Extraction screw conveyor 23 ... Input screw conveyor 24 ... Discharge screw conveyor 25 ... Blower 26 ... Electric heater 27 ... Bush 28 ... Bearing 29 ... Oil supply groove

Claims (1)

乾燥室内に、上下方向に多段に横方向に延長する内部にスクリューコンベアが内蔵された筒体が設けられると共に、各筒体は端部が上または下の筒体の端部と交互に連通されて一本に形成され、前記スクリューコンベアは往路と復路が上下に交互になるよう配設され、端部の筒体に乾燥室外に通じる投入口が設けられると共に、他の端部の筒体に乾燥室外に通じる排出口が設けられる乾燥装置において、スクリューコンベアのスクリュー軸は中空とし、一端はホウ金製のブッシュを介して軸受けで軸支され、軸受けの外周にはグリース注入用の給油溝を形成し、このスクリューコンベアのスクリュー軸の端部の軸受けを貫通してスクリュー軸内に電気ヒーターを配設したことを特徴とする汚泥等の乾燥装置。 In the drying chamber, there are provided cylinders with screw conveyors built in a multi-stage extending vertically in the vertical direction, and each cylinder is alternately communicated with the end of the upper or lower cylinder. The screw conveyor is arranged so that the forward path and the backward path are alternately arranged up and down, and the end cylinder is provided with a charging port leading to the outside of the drying chamber, and the other end cylinder is provided in the cylinder. In a drying device provided with a discharge port that leads to the outside of the drying chamber, the screw shaft of the screw conveyor is hollow, one end is supported by a bearing via a boring bush, and an oil supply groove for injecting grease is provided on the outer periphery of the bearing. An apparatus for drying sludge and the like, characterized in that an electric heater is disposed in the screw shaft through a bearing at the end of the screw shaft of the screw conveyor .
JP2007008007A 2007-01-17 2007-01-17 Sludge drying equipment Expired - Fee Related JP4505472B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104590921A (en) * 2015-01-23 2015-05-06 荣成海达鱼粉有限公司 Three-shaft-linked powder charging machine

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Publication number Priority date Publication date Assignee Title
WO2010001494A1 (en) * 2008-07-04 2010-01-07 睦和興業株式会社 Drying and carbonizing device
JP5152668B2 (en) * 2008-10-23 2013-02-27 睦和興業株式会社 Drying and carbonization equipment
JP6161952B2 (en) * 2013-05-13 2017-07-12 住友重機械工業株式会社 Fly ash transport device and fly ash transport method
CN107606922A (en) * 2017-09-07 2018-01-19 天津市启悦饲料有限责任公司 A kind of forage drier

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Publication number Priority date Publication date Assignee Title
JPS6027498A (en) * 1983-07-22 1985-02-12 Yoshiro Aoyama Screw press type sludge dehydrator
JPS61266379A (en) * 1985-05-18 1986-11-26 茨城環浄株式会社 Excrement agitating and transferring apparatus for compost producing excrement treatment facilities
JPH0938696A (en) * 1995-08-03 1997-02-10 Toshiba Mach Co Ltd Sludge treating device
JP2001004276A (en) * 1999-06-21 2001-01-12 Yoshida Tekko:Kk Garbage dryer
JP2002277165A (en) * 2001-03-16 2002-09-25 Hitachi Zosen Corp Screw-type heater

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Publication number Priority date Publication date Assignee Title
JPS6027498A (en) * 1983-07-22 1985-02-12 Yoshiro Aoyama Screw press type sludge dehydrator
JPS61266379A (en) * 1985-05-18 1986-11-26 茨城環浄株式会社 Excrement agitating and transferring apparatus for compost producing excrement treatment facilities
JPH0938696A (en) * 1995-08-03 1997-02-10 Toshiba Mach Co Ltd Sludge treating device
JP2001004276A (en) * 1999-06-21 2001-01-12 Yoshida Tekko:Kk Garbage dryer
JP2002277165A (en) * 2001-03-16 2002-09-25 Hitachi Zosen Corp Screw-type heater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104590921A (en) * 2015-01-23 2015-05-06 荣成海达鱼粉有限公司 Three-shaft-linked powder charging machine

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