JPH03284343A - Fluidized bed treatment apparatus - Google Patents

Fluidized bed treatment apparatus

Info

Publication number
JPH03284343A
JPH03284343A JP8617590A JP8617590A JPH03284343A JP H03284343 A JPH03284343 A JP H03284343A JP 8617590 A JP8617590 A JP 8617590A JP 8617590 A JP8617590 A JP 8617590A JP H03284343 A JPH03284343 A JP H03284343A
Authority
JP
Japan
Prior art keywords
fluidized bed
fluidizing
hot air
chamber
product discharge
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP8617590A
Other languages
Japanese (ja)
Inventor
Masao Tanaka
雅夫 田中
Naoji Sawaguchi
沢口 直司
Hideo Yamazaki
日出夫 山崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Okawara Mfg Co Ltd
Original Assignee
Okawara Mfg Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Okawara Mfg Co Ltd filed Critical Okawara Mfg Co Ltd
Priority to JP8617590A priority Critical patent/JPH03284343A/en
Publication of JPH03284343A publication Critical patent/JPH03284343A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/44Fluidisation grids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015Feeding of the particles in the reactor; Evacuation of the particles out of the reactor

Abstract

PURPOSE:To suitably discharge large particles generated in the treatment process by forming the draft openings located at least in the area facing to a product discharge opening among the draft openings located along the peripheral part of a fluidizing floor in such a way that hot air is blown out to the direction of the side wall of the fluidizing chamber. CONSTITUTION:The fluidizing floor 11 is provided to the bottom part of the fluidizing chamber 3. The process of drying, granulation, or coating, etc., is carried out by blowing up hot air from plural draft openings 12 formed in the fluidizing floor 11. The draft openings 12a located at least in the area facing to the product discharge opening 7 among the draft openings 12 located along the peripheral part of the fluidizing floor 11 are so formed that hot wind is flown out to the direction of the side wall of the fluidizing chamber 12. As a result, the large particles which are contained in the raw material or generated in the treatment process are suitably discharged. Consequently, a preferable fluidizing state is maintained, and the production efficiency is improved without useless work, such as the work of removing the remained material.

Description

【発明の詳細な説明】 (発明の目的) 〈産業上の利用分野) 本発明は流動層処理装置に関し、特に流動室内へ熱風を
送り込む際の熱風の吹き出し方向や吹き出し量を決定す
る流動床の改良に係るものである。
[Detailed Description of the Invention] (Objective of the Invention) (Industrial Application Field) The present invention relates to a fluidized bed processing device, and particularly to a fluidized bed treatment device that determines the direction and amount of hot air blown out when hot air is sent into a fluidized chamber. This is related to improvements.

(発明の背景〉 流動層処理装置は、流動室底部に設けた流動床の通気孔
から熱風を吹き込んで流動室内で粉粒体を流動化させて
、乾燥、造粒、コーティングなどの処理を行なうもので
ある。このまうな流動層処理装置で乾燥、造粒、コーテ
ィングなどの処理を行なう場合には、原料中に混在し、
あるいは処理過程で生ずる大粒子(いわゆるダマ)を適
宜流動室から排出してやらないと、流動が阻害されると
いう問題が発生する。とりわけ連続処理の場合には、こ
の大粒子の排出がうまくいかないと、逐次流動床上に蓄
積されてゆき、最悪の場合流動停止といった事態になっ
てしまう、このため、従来、流動室内に回転攪拌翼を設
けて掻き出すようにしたものや、方向性をもった通気孔
を穿った流動床を用いて、これによって生ずる気流の遠
心力によって大粒子を排出しようとするものがあった。
(Background of the invention) A fluidized bed treatment device fluidizes powder and granules in the fluidization chamber by blowing hot air through the ventilation holes of the fluidized bed provided at the bottom of the fluidization chamber, and performs processes such as drying, granulation, and coating. When performing processes such as drying, granulation, and coating using this sophisticated fluidized bed processing equipment,
Alternatively, unless large particles (so-called lumps) generated during the treatment process are properly discharged from the flow chamber, a problem arises in that the flow is obstructed. Particularly in the case of continuous processing, if these large particles are not properly discharged, they will accumulate on the fluidized bed one after another, and in the worst case, the fluidization will stop.For this reason, conventionally, rotating stirring blades were installed in the fluidizing chamber. Some used a fluidized bed with directional ventilation holes to eject large particles using the centrifugal force of the resulting airflow.

しかしながら、このような方法によっても大粒子はある
程度流動室側壁の方へ寄せられていくが、大粒子を効率
よく排出することはできない、これには次のような理由
が考えられる。即ち流動室内で粉粒体は、主に中心部か
ら吹き上げられ、側壁部に沿って下降し、中心部に向か
う、このような大量の粉粒体が影響して、大粒子が流動
室側壁部に設けた排出口まで到達することができないの
である。
However, even with such a method, large particles are brought toward the side wall of the flow chamber to some extent, but the large particles cannot be efficiently discharged.The following reasons can be considered for this. In other words, in the flow chamber, the powder and granules are mainly blown up from the center, descend along the side walls, and head toward the center.As a result of this large amount of powder and granules, large particles flow up to the side walls of the flow chamber. It is not possible to reach the outlet provided in the

〈開発を試みた技術的事項) 本発明はこのような背景に鑑みなされたものであって、
流動床を改良することにより、原料中に混在し、あるい
は処理過程で生ずる大粒子を適宜排出できるようにした
流動層処理装置の開発を試みたものである。
(Technical matters attempted to be developed) The present invention was made in view of this background, and
This is an attempt to develop a fluidized bed treatment device that can appropriately discharge large particles mixed in raw materials or generated during the treatment process by improving the fluidized bed.

(発明の構成) (目的達成の手段) 即ち本出願に係る流動層処理装置は、流動室底部に流動
床を設け、この流動床に複数形成される通気孔から熱風
を吹き上げて乾燥、造粒、コーティングなどの操作を行
なう装置において、前記流動床における周縁部の通気孔
のうち少なくとも製品排出口に臨む範囲の通気孔は、流
動室側壁方向へ向かって熱風が吹き出すように形成され
ていることを特徴とするものであり、もって前記目的を
達成しようとするものである。
(Structure of the Invention) (Means for Achieving the Object) That is, the fluidized bed processing apparatus according to the present application has a fluidized bed provided at the bottom of the fluidized chamber, and hot air is blown up from a plurality of ventilation holes formed in the fluidized bed for drying and granulation. In an apparatus for performing operations such as coating, at least the vents in the area facing the product discharge port among the vent holes in the peripheral portion of the fluidized bed are formed so that hot air is blown toward the side wall of the fluidizing chamber. The present invention is characterized by the following, and aims to achieve the above object.

(発明の作用〉 本発明にあっては、流動床における周縁部の通気孔のう
ち少なくとも製品排出口に臨む範囲の通気孔は、流動室
側壁方向へ向かって熱風が吹き出すように形成したから
、原料中に混在し、あるいは処理過程で生ずる大粒子は
、粉粒体の流れによる影響に反して製品排出口がら排出
される。
(Function of the Invention) In the present invention, at least the vents in the area facing the product discharge port among the vents in the peripheral portion of the fluidized bed are formed so that hot air blows out toward the side wall of the fluidized chamber. Large particles mixed in the raw materials or generated during the processing process are discharged from the product discharge port against the influence of the flow of powder and granules.

(実施例〉 以下本発明を図示の実施例に基づいて具体的に説明する
。符号1は本発明たる流動層処理装置であって、このも
のはその上部を構成するほぼ円筒状の流動室3に対して
、熱風供給部6及び製品排出ロアを設けて成るものであ
る。流動室3は粉粒体を流動させるところであり、その
ほぼ中央部には流動室3の側壁から内側に向がって一例
として三本の導管8を設け、この導管8の先端部にノズ
ル9が取り付けられる。因みにこのノズル9からは、造
粒時にはバインダ液が噴霧され、またコーティング時に
はコーテイング液が噴霧されて、それぞれ流動中の粉粒
体にふり掛けられることにより、造粒、コーティング処
理がなされる。尚、乾燥処理の場合にはこのノズル9は
使用されない、熱風供給部6は流動室3内へ流動用の熱
風を供給するための部分であって、流動層処理装置1の
最下部に熱風供給室10を具えて成る。また熱風供給部
6と流動室3との境界部には流動床11を設ける。
(Example) The present invention will be explained in detail below based on the illustrated example. Reference numeral 1 denotes a fluidized bed treatment apparatus according to the present invention, which has a substantially cylindrical fluid chamber 3 constituting the upper part thereof. In contrast, a hot air supply section 6 and a product discharge lower are provided.The fluidization chamber 3 is a place for fluidizing the powder and granules, and approximately in the center thereof there is a wall extending inward from the side wall of the fluidization chamber 3. As an example, three conduits 8 are provided, and a nozzle 9 is attached to the tip of the conduit 8. Incidentally, from these nozzles 9, a binder liquid is sprayed during granulation, and a coating liquid is sprayed during coating. Granulation and coating are performed by sprinkling them onto the flowing powder and granules.In addition, in the case of drying, this nozzle 9 is not used, and the hot air supply section 6 is used to flow into the fluidizing chamber 3. The hot air supply chamber 10 is provided at the bottom of the fluidized bed treatment apparatus 1. A fluidized bed 11 is provided at the boundary between the hot air supply section 6 and the fluidized chamber 3. .

この流動床11は、熱風供給室lOから流動室3内へ送
られる熱風の量や向きを規制するためのものであって、
第1.2図に示すように全体が円盤状で、その表面には
複数の通気孔12を形成して成る。本発明はこのような
通気孔12の向きに特徴を有するものであって、流動床
11の周縁部の通気孔12のうち、少なくとも製品排出
ロアに臨む範囲の通気孔12は、流動室3の側壁方向へ
向かって熱風が吹き出すように形成されている。このよ
うに製品排出ロアに臨む範囲の通気孔を以下通気孔12
aと表し、他の通気孔12と区別する。因みに製品排出
ロアに臨む範囲の通気孔12aを流動室3の側壁方向へ
向かって熱風が吹き出すように形成すれば。
This fluidized bed 11 is for regulating the amount and direction of hot air sent from the hot air supply chamber IO into the fluidized chamber 3,
As shown in Fig. 1.2, the entire body is disk-shaped, and a plurality of ventilation holes 12 are formed on its surface. The present invention is characterized by the direction of the ventilation holes 12, and among the ventilation holes 12 at the peripheral edge of the fluidized bed 11, at least the ventilation holes 12 in the range facing the product discharge lower are in the direction of the fluidization chamber 3. It is formed so that hot air blows out toward the side wall. The ventilation holes in the area facing the product discharge lower are shown below as ventilation holes 12.
a to distinguish it from other ventilation holes 12. Incidentally, if the ventilation hole 12a in the area facing the product discharge lower is formed so that hot air blows out toward the side wall of the flow chamber 3.

熱風が製品排出ロアに向かって吹き出すため、流動床1
1上の排出口近傍に滞溜する大粒子は。
Because the hot air blows toward the product discharge lower, the fluidized bed 1
The large particles that accumulate near the discharge port on 1.

常時排出ロアへ押しやられて排出される。ここでこのよ
うな通気孔12の形成態様として、第2図(a)〜(c
)に示す態様を採ることができる。
It is constantly pushed to the discharge lower and discharged. Here, as the formation mode of such a ventilation hole 12, FIGS. 2(a) to 2(c)
) can be adopted.

第2図(a)に示すものは、流動床の周縁部であって製
品排出ロアに面した範囲における通気孔12aを、流動
室の側壁に向がって熱風が吹き出すように形成し、他の
範囲の通気孔12は、円形の流動床の接線方向に向がっ
て熱風が吹き出すように形成したものである。尚、少な
くとも製品排出ロアに面した範囲の通気孔12aが流動
室の側壁に向かって熱風が吹き出すように形成されてい
ればよいのであって、例えば他の範囲の通気孔12につ
いても側壁方向に向けて形成されていてもよい、また第
2図(b)に示すものは、すべての通気孔12,12a
が製品排出ロアに向かって熱風を吹き出すように形成し
たものである。尚この場合、実質的に製品排出ロア近傍
に滞溜する大粒子に熱風を送り大粒子を押しやって排出
する作用をする通気孔12を特定することは必ずしもで
きないが1図中では便宜上製品排出ロアに最も近いもの
を通気孔12aとして表す、更に第2図(c)に示すも
のは。
In the case shown in FIG. 2(a), vent holes 12a in the peripheral edge of the fluidized bed facing the product discharge lower are formed so that hot air blows out toward the side wall of the fluidized chamber. The ventilation holes 12 in the range are formed so that hot air blows out in the tangential direction of the circular fluidized bed. It is sufficient that at least the ventilation holes 12a in the range facing the product discharge lower are formed so that hot air blows out toward the side wall of the flow chamber. In the case shown in FIG. 2(b), all the ventilation holes 12, 12a
is designed to blow hot air toward the product discharge lower. In this case, it is not necessarily possible to specify the ventilation hole 12 that actually sends hot air to the large particles accumulated near the product discharge lower, pushes the large particles, and discharges them. The one closest to the one shown in FIG. 2(c) is represented as the vent hole 12a.

流動床の直上に回転する攪拌翼13を具え、製品排出ロ
アに面した範囲には流動室の側壁に向かって熱風が吹き
出すように通気孔12aを形成すると共に、それ以外の
範囲にはパンチングあるいは金網状の通気孔12を形成
したものである0次に製品排出ロアは、造粒等の処理が
なされた製品を取り出すと共に、いわゆる大粒子の排出
もここから行なわれる。尚、製品と大粒子との分級は、
製品排出ロアの後工程に設けられる分級装置等によって
適宜性なわれる。また流動室3に対して製品排出ロアを
設ける方向は、製品排出ロアを設ける箇所の流動室3の
水平断面を考えた場合、第3図(a)に示すように断面
たる円の接線と垂直方向に設ける他、第3図(b)に示
すように断面たる円の接線方向に設けるようにしてもよ
い、因みにこのような方向に製品排出ロアを配設すれば
、流動室3内において造粒物や粉粒体が旋回するように
流動しているから、その流れに沿うようにして容易に造
粒物を製品排出ロアへ導くことができる。
A rotating stirring blade 13 is provided directly above the fluidized bed, and ventilation holes 12a are formed in the area facing the product discharge lower so that hot air is blown toward the side wall of the fluidization chamber, and punching or other holes are formed in the other area. The zero-order product discharge lower, which is formed with a wire-mesh-like ventilation hole 12, takes out products that have been subjected to processes such as granulation, and also discharges so-called large particles. In addition, the classification of products and large particles is as follows:
Appropriateness is determined by a classification device, etc. installed in the downstream process of the product discharge lower. Furthermore, when considering the horizontal cross section of the flow chamber 3 where the product discharge lower is installed, the direction in which the product discharge lower is provided with respect to the flow chamber 3 is perpendicular to the tangent of the circle that is the cross section, as shown in Figure 3 (a). In addition to providing it in the direction, it may also be provided in the tangential direction of the circle that is the cross section as shown in FIG. Since the granules and granules flow in a swirling manner, the granules can be easily guided to the product discharge lower along the flow.

本発明たる流動層処理装置1は以上述べたような構造を
有するものであって、以下このものの使用状態について
連続造粒操作を例にとって説明する。まず原料たる粉粒
体が連続的に流動室3内に供給され一定量に達すると、
熱風供給室10かも熱風が送られると共に、バインダ液
がノズル9から噴霧される。これにより粉粒体が流動室
3内を流動しながらバインダ液の作用にまり造粒がなさ
れる。この造粒過程では、あらかじめ原料中に混在した
り、造粒過程で生ずる大粒子が流動床上に蓄積されがち
であるが。
The fluidized bed processing apparatus 1 of the present invention has the structure as described above, and the usage state of this apparatus will be explained below by taking a continuous granulation operation as an example. First, powder or granular material as a raw material is continuously supplied into the flow chamber 3, and when it reaches a certain amount,
Hot air is also sent to the hot air supply chamber 10, and the binder liquid is sprayed from the nozzle 9. As a result, the powder particles flow in the flow chamber 3 and are granulated by the action of the binder liquid. In this granulation process, large particles that are mixed in the raw materials or generated during the granulation process tend to accumulate on the fluidized bed.

かかる大粒子は製品排出ロアに臨む範囲に形成された通
気孔12aがら吹き出される熱風により製品排出ロアか
ら排出される。
Such large particles are discharged from the product discharge lower by hot air blown out through the ventilation hole 12a formed in the area facing the product discharge lower.

(発明の効果) 本発明にあっては、流動床11における周縁部の通気孔
12のうち、少なくとも製品排出ロアに臨む範囲の通気
孔12aを流動室3の側壁方向へ向かって熱風が吹き出
すように形成しであるので、原料中に混在し、あるいは
処理過程で生ずる大粒子は、製品排出ロアに向かって押
しやられる。そのため、このような大粒子は。
(Effects of the Invention) In the present invention, hot air is blown out toward the side wall of the fluidized chamber 3 through at least the vents 12a in the range facing the product discharge lower among the vents 12 at the peripheral edge of the fluidized bed 11. Therefore, large particles mixed in the raw materials or generated during the processing process are pushed toward the product discharge lower. Therefore, such large particles.

流動室中央部から吹き上げられ、側壁に沿って下降して
中央部に向かう粉粒体の循環運動の力に勝って製品排出
ロアから排出される。これにより良好な流動状態が維持
でき、滞溜物の排除などの無駄な作業がなくなり製造効
率が向上する。また流動状態が良くなれば、造粒時にお
いては大径の粒ができることも少なくなり、また乾燥時
においては局部的な乾燥ムラを生じることもなくなるた
め、良好な製品が得られる。更にこのような効果は、連
続処理を行なう場合に一層顕著である。
The powder is blown up from the center of the fluidization chamber, descends along the side walls, and is discharged from the product discharge lower by overcoming the force of the circulating movement of the powder and granules toward the center. This allows a good fluidity state to be maintained, eliminating wasteful work such as removing stagnant matter, and improving manufacturing efficiency. In addition, if the fluidity is improved, large-diameter particles are less likely to be formed during granulation, and local unevenness in drying is also prevented during drying, resulting in a better product. Furthermore, such effects are even more pronounced when continuous processing is performed.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の流動層処理装置を示す分解斜視図、第
2図は流動床に形成する通気孔の種々の形態を示す平面
図、第3図は製品排出口の取り付は位置を異ならせた二
種の実施例を示す横断面図である。 1;流動層処理装置 3;流動室 6;熱風供給部 7;製品排出口 8;導管 9・ノズル 10・熱風供給室 11・流動床 12・通気孔 12a;通気孔 13;攪拌翼 ((7) (b)
Fig. 1 is an exploded perspective view showing the fluidized bed processing apparatus of the present invention, Fig. 2 is a plan view showing various forms of ventilation holes formed in the fluidized bed, and Fig. 3 shows the installation position of the product discharge port. FIG. 3 is a cross-sectional view showing two different embodiments. 1; Fluidized bed treatment device 3; Fluidization chamber 6; Hot air supply section 7; Product discharge port 8; Conduit 9, nozzle 10, Hot air supply chamber 11, Fluidized bed 12, Vent hole 12a; Vent hole 13; Stirring blade ((7 ) (b)

Claims (1)

【特許請求の範囲】[Claims]  流動室底部に流動床を設け、この流動床に複数形成さ
れる通気孔から熱風を吹き上げて乾燥、造粒、コーティ
ングなどの操作を行なう装置において、前記流動床にお
ける周縁部の通気孔のうち少なくとも製品排出口に臨む
範囲の通気孔は、流動室側壁方向へ向かって熱風が吹き
出すように形成されていることを特徴とする流動層処理
装置。
In an apparatus in which a fluidized bed is provided at the bottom of the fluidized bed and hot air is blown up from a plurality of vent holes formed in the fluidized bed to perform operations such as drying, granulation, coating, etc., at least one of the vent holes at the peripheral edge of the fluidized bed A fluidized bed processing apparatus characterized in that the ventilation holes in the area facing the product discharge port are formed so that hot air is blown out toward the side wall of the fluidization chamber.
JP8617590A 1990-03-30 1990-03-30 Fluidized bed treatment apparatus Pending JPH03284343A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8617590A JPH03284343A (en) 1990-03-30 1990-03-30 Fluidized bed treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8617590A JPH03284343A (en) 1990-03-30 1990-03-30 Fluidized bed treatment apparatus

Publications (1)

Publication Number Publication Date
JPH03284343A true JPH03284343A (en) 1991-12-16

Family

ID=13879424

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8617590A Pending JPH03284343A (en) 1990-03-30 1990-03-30 Fluidized bed treatment apparatus

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002028466A (en) * 2000-05-10 2002-01-29 Mitsubishi Chemicals Corp Granular particles treatment device and producing method for coated fertilizer
JP2002292266A (en) * 2001-03-30 2002-10-08 Okawara Mfg Co Ltd Fluidized bed granulation drier facilitating flow of object to be treated
JP2016519749A (en) * 2013-04-03 2016-07-07 グラット インジェニェーアテヒニク ゲゼルシャフト ミット ベシュレンクテル ハフツングGlatt Ingenieurtechnik GmbH Fluidization equipment
US10132565B2 (en) 2013-04-03 2018-11-20 Glatt Ingenieurtechnik Gmbh Rotary dryer star and method for treating solid particles

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002028466A (en) * 2000-05-10 2002-01-29 Mitsubishi Chemicals Corp Granular particles treatment device and producing method for coated fertilizer
JP2002292266A (en) * 2001-03-30 2002-10-08 Okawara Mfg Co Ltd Fluidized bed granulation drier facilitating flow of object to be treated
JP2016519749A (en) * 2013-04-03 2016-07-07 グラット インジェニェーアテヒニク ゲゼルシャフト ミット ベシュレンクテル ハフツングGlatt Ingenieurtechnik GmbH Fluidization equipment
US10076738B2 (en) 2013-04-03 2018-09-18 Glatt Ingenieurtechnick GmbH Fluidizing device
US10132565B2 (en) 2013-04-03 2018-11-20 Glatt Ingenieurtechnik Gmbh Rotary dryer star and method for treating solid particles

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