JP6625479B2 - Flash dryer - Google Patents

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JP6625479B2
JP6625479B2 JP2016093598A JP2016093598A JP6625479B2 JP 6625479 B2 JP6625479 B2 JP 6625479B2 JP 2016093598 A JP2016093598 A JP 2016093598A JP 2016093598 A JP2016093598 A JP 2016093598A JP 6625479 B2 JP6625479 B2 JP 6625479B2
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drying
flash
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dried
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晃一 山上
晃一 山上
仁司 輪達
仁司 輪達
吉川 知久
知久 吉川
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Taiheiyo Cement Corp
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Description

本発明は、気流乾燥機に関し、特に、粗粒を含む高含水物を乾燥させる気流乾燥機に関する。   BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a flash dryer, and more particularly, to a flash dryer for drying a high water content containing coarse particles.

特許文献1には、乾燥対象物に含まれる鉄片等の重量物を比重差選別しながら空気流により乾燥対象物を乾燥させ、重量物除去後の乾燥対象物を渦状の空気流でさらに乾燥させる気流乾燥機が開示されている。   Patent Literature 1 discloses that an object to be dried is dried by an air flow while a heavy object such as an iron piece included in the object to be dried is selectively sorted, and the object to be dried after removing the heavy object is further dried by a vortex air flow. A flash dryer is disclosed.

また、特許文献2には、乾燥対象物に含まれる比重の大きなものを選別しながら乾燥対象物を熱風によって乾燥させ、比重の大きなものが分離された後の乾燥対象物を熱風によってさらに乾燥させる気流乾燥機が開示される。   Further, in Patent Literature 2, a drying target is dried with hot air while selecting a high specific gravity contained in the drying target, and the drying target after the large specific gravity is separated is further dried with hot air. A flash dryer is disclosed.

特開2000−304439号公報JP 2000-304439 A 特開2012−180943号公報JP 2012-180943 A

上記特許文献1及び2に記載の気流乾燥機では、乾燥対象物に含まれる重量物等の塊状物を分離することで、塊状物が気流乾燥機内に残留し続ける事態を回避することができるものの、比重差選別による落下物の中には、乾燥が不十分で、水分の重さにより落下した微粒も含まれており、上記特許文献1及び2は、この乾燥が不十分な微粒について考慮しておらず、改善の余地があった。   In the flash dryers described in Patent Documents 1 and 2, although a lump such as a heavy substance contained in a drying target is separated, it is possible to avoid a situation in which the lump remains in the flash dryer. In addition, among the fallen objects due to the specific gravity difference sorting, fine particles that are insufficiently dried and fall due to the weight of moisture are also included. The above Patent Documents 1 and 2 consider the fine particles that are insufficiently dried. There was room for improvement.

そこで、本発明は、上記従来の技術における問題点に鑑みてなされたものであって、塊状物(以下「粗粒」という。)を含む高含水物等の乾燥対象物を効率よく乾燥させることが可能な気流乾燥機を提供することを目的とする。   Therefore, the present invention has been made in view of the above-mentioned problems in the related art, and is intended to efficiently dry a drying target such as a high water content including a lump (hereinafter, referred to as “coarse particles”). It is an object of the present invention to provide a flash dryer capable of performing the following.

上記目的を達成するため、本発明は気流乾燥機であって、乾燥対象物を乾燥用ガスの気流によって乾燥させる気流乾燥部と、前記気流乾燥部から落下する落下物を選別する篩と、該篩の通過物を前記気流乾燥部に戻すルートと、前記篩の残分を機外に排出するルートとを備えることを特徴とする。   In order to achieve the above object, the present invention is a flash dryer, which is a flash dryer for drying an object to be dried by an airflow of a drying gas, a sieve for sorting falling objects falling from the flash dryer, It is characterized by comprising a route for returning the material passed through the sieve to the flash drying unit, and a route for discharging the residue of the sieve outside the machine.

本発明に係る気流乾燥機によれば、気流乾燥部からの落下物を篩によって選別するため、乾燥が不十分な微粒を粗粒として機外へ排出することがなく、粗粒を含む乾燥対象物を効率よく乾燥させることができる。   According to the flash dryer according to the present invention, since the falling objects from the flash drying section are sorted by the sieve, the fine particles that are not sufficiently dried are not discharged to the outside as coarse particles, and the drying target including the coarse particles is not removed. The object can be dried efficiently.

上記気流乾燥機において、前記気流乾燥部は、乾燥物を前記乾燥用ガスと共に排出することができる。   In the flash dryer, the flash drying unit may discharge the dried product together with the drying gas.

また、前記乾燥対象物と乾燥用ダストを混合撹拌しながら前記気流乾燥部に搬送する乾燥搬送部を設けることができ、前記気流乾燥部を、前記乾燥搬送部からの混合物を乾燥させるように構成することができる。これにより、乾燥対象物をより効率よく乾燥させることができる。さらに乾燥効率を向上させるため、前記篩の通過物を前記気流乾燥部に戻すルートに代えて、前記篩の通過物を前記乾燥搬送部に戻すルートを設けてもよい。   Further, it is possible to provide a drying / transporting unit that transports the drying target and the drying dust to the flash drying unit while mixing and stirring the drying target, and the flash drying unit is configured to dry the mixture from the drying / transporting unit. can do. Thereby, the object to be dried can be dried more efficiently. In order to further improve the drying efficiency, a route for returning the passing material of the sieve to the drying and conveying unit may be provided instead of the route for returning the passing material of the sieve to the flash drying unit.

以上のように、本発明によれば、粗粒を含む乾燥対象物を効率よく乾燥させることが可能な気流乾燥機を提供することが可能となる。   As described above, according to the present invention, it is possible to provide a flash dryer capable of efficiently drying a drying target including coarse particles.

本発明に係る気流乾燥機の一実施の形態を示す概略図である。It is the schematic which shows one Embodiment of the flash dryer which concerns on this invention.

次に、本発明に係る気流乾燥機の一実施の形態について、図1を参照しながら説明する。尚、同図において、実線の矢線は固体の流れを、破線の矢線は気体の流れを示す。   Next, an embodiment of a flash dryer according to the present invention will be described with reference to FIG. In the figure, the solid arrow indicates the flow of the solid, and the broken arrow indicates the flow of the gas.

この気流乾燥機1は、乾燥対象物Oと乾燥用ダストD1を混合撹拌しながら搬送する乾燥搬送部2と、乾燥搬送部2からの混合物Mを乾燥用ガスGの気流によって乾燥させる気流乾燥部3と、気流乾燥部3から落下する落下物Fを選別する篩4と、篩4の通過物を乾燥搬送部2に戻すルート5とで構成される。   The flash dryer 1 includes a drying transport unit 2 that transports the drying object O and the drying dust D1 while mixing and stirring the same, and a flash drying unit that dries the mixture M from the drying transport unit 2 by a stream of the drying gas G. 3, a sieve 4 for selecting the falling objects F falling from the flash drying unit 3, and a route 5 for returning the passing material of the sieve 4 to the drying and conveying unit 2.

乾燥搬送部2は、乾燥対象物Oと乾燥用ダストD1が供給される供給口2aと、混合物Mを排出する排出口2bと、図示しない駆動源によって回転する回転軸2cと、回転軸2cに間隔を空けて複数設置されるパドル2dとを備える。尚、パドル2dに代えてスクリューを設けてもよい。   The drying / conveying unit 2 includes a supply port 2a through which the drying target O and the drying dust D1 are supplied, a discharge port 2b that discharges the mixture M, a rotating shaft 2c rotated by a drive source (not shown), and a rotating shaft 2c. And a plurality of paddles 2d provided at intervals. Note that a screw may be provided instead of the paddle 2d.

気流乾燥部3は、上部3aが直方体状、下部3bが角錐台状の内部空間を有する部屋状に形成される。上部3aの右側面に乾燥用ガスGの流入口3cと、左側面に乾燥搬送部2からの混合物Mが供給される供給口3dと、天井部に排ガスG1及び微粒D2を排出する排気口3eとが設けられる。図示の例では、排気口3eは気流乾燥部3の上部に形成されているが、気流乾燥部3の側部に設けてもよい。一方、下部3bの下端部には、混合物Mのうち微粒D2以外のもの(落下物F)を排出する排出口3fが形成される。   The flash drying unit 3 is formed in a room shape having an internal space in which the upper part 3a has a rectangular parallelepiped shape and the lower part 3b has a truncated pyramid shape. An inlet 3c for the drying gas G is provided on the right side of the upper portion 3a, a supply port 3d for supplying the mixture M from the drying transfer section 2 on the left side, and an exhaust port 3e for discharging the exhaust gas G1 and the fine particles D2 on the ceiling. Are provided. In the illustrated example, the exhaust port 3 e is formed above the flash drying unit 3, but may be provided on the side of the flash drying unit 3. On the other hand, at the lower end of the lower part 3b, an outlet 3f for discharging the mixture M other than the fine particles D2 (falling object F) is formed.

篩4は、気流乾燥部3から落下する落下物Fを効率よく選別することができればよく、振動篩等の各種の篩を乾燥対象物Oに応じて適宜選択することができる。   The sieve 4 only needs to be able to efficiently sort the falling objects F falling from the flash drying unit 3, and various sieves such as a vibrating sieve can be appropriately selected according to the drying target O.

上記構成を有する気流乾燥機1の動作について、図1を参照しながら詳細に説明する。   The operation of the flash dryer 1 having the above configuration will be described in detail with reference to FIG.

乾燥搬送部2の供給口2aに乾燥対象物Oと乾燥用ダストD1を供給し、これらを混合撹拌しながら搬送する。これによって、気流乾燥の前に乾燥対象物Oをある程度乾燥させることができる。乾燥対象物Oは、含水した粘土系廃棄物、農業系・漁業系残渣等の高含水物である。乾燥用ダストD1には、熱量を有する上記微粉D2、セメントキルンダスト等を用いることができ、乾燥用ダストD1の温度や供給量は、乾燥対象物Oの量や含水率に応じて適宜設定される。   The drying object O and the drying dust D1 are supplied to the supply port 2a of the drying and transporting unit 2 and are transported while mixing and stirring them. Thereby, the drying target O can be dried to some extent before flash drying. The object to be dried O is a highly hydrated material such as hydrated clay-based waste and agricultural / fishery residue. As the drying dust D1, the fine powder D2 having a calorific value, a cement kiln dust, or the like can be used. You.

乾燥搬送部2で混合撹拌された混合物Mを排出口2b及び供給口3dを介して気流乾燥部3へ供給し、流入口3cから流入した乾燥用ガスGの気流によって乾燥させる。乾燥用ガスGの温度や流速は、混合物Mの量や含水率に応じて適宜設定される。   The mixture M mixed and stirred in the drying / conveying section 2 is supplied to the flash drying section 3 through the outlet 2b and the supply port 3d, and is dried by the stream of the drying gas G flowing from the inlet 3c. The temperature and the flow rate of the drying gas G are appropriately set according to the amount of the mixture M and the water content.

乾燥搬送部2で乾燥用ガスGによって乾燥された混合物M中の微粒D2は、排ガスG1と共に排気口3eから排出される。一方、混合物Mのうち気流乾燥部3から落下する落下物Fは、排出口3fを介して篩4に達し、篩4を通過する微粒D3と、篩4上に残留する塊状物Bとに選別される。尚、篩4の目開きは乾燥対象物Oに応じて適宜設定される。   The fine particles D2 in the mixture M dried by the drying gas G in the drying transport unit 2 are discharged from the exhaust port 3e together with the exhaust gas G1. On the other hand, the falling matter F falling from the flash drying unit 3 of the mixture M reaches the sieve 4 through the discharge port 3f, and is separated into fine particles D3 passing through the sieve 4 and lumps B remaining on the sieve 4. Is done. The opening of the sieve 4 is appropriately set according to the drying target O.

微粒D3は、気流乾燥部3での乾燥が不十分であったために水分を含み、その水分の重さにより落下物Fに含まれてしまったものであって、本来は乾燥物として微粒D2と共に回収されるべきものであるため、ルート5を介して乾燥搬送部2へ戻して再度乾燥される。一方、塊状物Bは機外へ排出する。   The fine particles D3 contain water due to insufficient drying in the flash drying unit 3 and are included in the falling object F due to the weight of the water, and are originally dried together with the fine particles D2. Since it is to be collected, it is returned to the drying / conveying unit 2 via the route 5 and dried again. On the other hand, the lump B is discharged outside the machine.

以上のように、本実施の形態によれば、気流乾燥部3からの落下物Fを篩4によって選別するため、乾燥が不十分な微粒D3を塊状物Bとして除去することがなく、粗粒を含む乾燥対象物Oを効率よく乾燥させることができる。   As described above, according to the present embodiment, since the falling object F from the flash drying unit 3 is sorted by the sieve 4, the fine particles D3 that are insufficiently dried are not removed as the lump B, and the coarse particles D are not removed. Can be efficiently dried.

尚、上記実施の形態においては、乾燥搬送部2を設けた場合について説明したが、乾燥対象物Oの含水率によっては乾燥搬送部2を設けずに、乾燥対象物Oを直接気流乾燥部3に供給することもできる。また、乾燥搬送部2を備える気流乾燥機1であっても、微粒D3の含水率が低い場合には、微粒D3をルート5を介して乾燥搬送部2へ戻さずに、直接気流乾燥部3に戻してもよい。   In the above embodiment, the case where the drying and conveying unit 2 is provided has been described. However, depending on the water content of the drying object O, the drying object O is directly provided without the drying and conveying unit 2 and the flash drying unit 3 Can also be supplied. Even in the flash dryer 1 including the drying and conveying unit 2, when the moisture content of the fine particles D3 is low, the fine particles D3 are not returned to the drying and conveying unit 2 via the route 5 but directly to the flash drying unit 3. May be returned.

1 気流乾燥機
2 乾燥搬送部
2a 供給口
2b 排出口
2c 回転軸
2d パドル
3 気流乾燥部
3a 上部
3b 下部
3c 流入口
3d 供給口
3e 排気口
3f 排出口
4 篩
5 ルート
B 塊状物
D1 乾燥用ダスト
D2、D3 微粒
F 落下物
G 乾燥用ガス
G1 排ガス
M 混合物
O 乾燥対象物
DESCRIPTION OF SYMBOLS 1 Flash dryer 2 Dry conveyance part 2a Supply port 2b Discharge port 2c Rotating shaft 2d Paddle 3 Pneumatic drying part 3a Upper part 3b Lower part 3c Inlet 3d Supply port 3e Exhaust port 3f Discharge port 4 Sieve 5 Route B Lump D1 Dry dust D2, D3 Fine particles F Falling object G Drying gas G1 Exhaust gas M Mixture O Drying object

Claims (4)

乾燥対象物を乾燥用ガスの気流によって乾燥させる気流乾燥部と、
該気流乾燥部から落下する落下物を選別する篩と、
該篩の通過物を前記気流乾燥部に戻すルートと、
前記篩の残分を機外に排出するルートとを備えることを特徴とする気流乾燥機。
A flash drying unit for drying a drying target by a flow of a drying gas,
A sieve for sorting falling objects falling from the flash drying unit;
A route for returning the passing material of the sieve to the flash drying unit;
And a route for discharging the residue of the sieve outside the machine.
前記気流乾燥部は、乾燥物を前記乾燥用ガスと共に排出することを特徴とする請求項1に記載の気流乾燥機。   The flash dryer according to claim 1, wherein the flash drying unit discharges a dried product together with the drying gas. 前記乾燥対象物と乾燥用ダストを混合撹拌しながら前記気流乾燥部に搬送する乾燥搬送部を備え、
前記気流乾燥部は、前記乾燥搬送部からの混合物を乾燥させることを特徴とする請求項1又は2に記載の気流乾燥機。
A drying and conveying unit that conveys the drying target and the drying dust to the flash drying unit while mixing and stirring,
The flash dryer according to claim 1, wherein the flash drying unit dries the mixture from the drying transport unit.
前記篩の通過物を前記気流乾燥部に戻すルートに代えて、前記篩の通過物を前記乾燥搬送部に戻すルートを備えることを特徴とする請求項3に記載の気流乾燥機。   4. The flash dryer according to claim 3, further comprising a route that returns the passed material of the sieve to the drying and conveying unit, instead of a route of returning the passed material of the sieve to the flash drying unit. 5.
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