JPH0652929U - Processing liquid supply device for particle processing equipment - Google Patents

Processing liquid supply device for particle processing equipment

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Publication number
JPH0652929U
JPH0652929U JP8878792U JP8878792U JPH0652929U JP H0652929 U JPH0652929 U JP H0652929U JP 8878792 U JP8878792 U JP 8878792U JP 8878792 U JP8878792 U JP 8878792U JP H0652929 U JPH0652929 U JP H0652929U
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JP
Japan
Prior art keywords
processing
flow path
spray nozzle
gas flow
processing container
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.)
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Application number
JP8878792U
Other languages
Japanese (ja)
Inventor
浩 坂本
勝弘 井上
秀一 土岐
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Powrex KK
Original Assignee
Powrex KK
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Publication date
Application filed by Powrex KK filed Critical Powrex KK
Priority to JP8878792U priority Critical patent/JPH0652929U/en
Publication of JPH0652929U publication Critical patent/JPH0652929U/en
Withdrawn legal-status Critical Current

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Abstract

(57)【要約】 【目的】 液滴の噴霧方向を変更自在とすると共に、ス
プレーゾーンの形成領域を広く確保して液滴及び粉粒体
の早期の接触を確実に防止する。 【構成】 球体状をなす揺動部材(15)に貫通孔(16)
を形成し、この貫通孔(16)の一端部に末広がりの拡径
部(17)を設ける。この貫通孔(16)内には、揺動部材
(15)の内径面との間に環状隙間を設け、且つ、噴射口
(21)を拡径部(17)の開口(17a)より後退させてス
プレーノズル(20)を収納する。揺動部材(15)とスプ
レーノズル(20)の間には、二次気体流路(36)を形成
する。この二次気体流路(36)の一端部は二次空気供給
源に連結し、他端部は拡径部(17)に連通させる。この
揺動部材(15)を、内径面を連続凹状球面に形成した案
内部材(41)で支持する。
(57) [Summary] [Objective] The spray direction of droplets can be freely changed, and a wide spray zone formation area is ensured to prevent early contact between droplets and granular material. [Structure] Through hole (16) in swing member (15) having a spherical shape
And a diametrically expanded portion (17) diverging toward the end is provided at one end of the through hole (16). An annular gap is provided between the through hole (16) and the inner diameter surface of the swing member (15), and the injection port (21) is retracted from the opening (17a) of the expanded diameter portion (17). The spray nozzle (20). A secondary gas flow path (36) is formed between the swing member (15) and the spray nozzle (20). One end of the secondary gas flow path (36) is connected to the secondary air supply source, and the other end of the secondary gas flow path (36) communicates with the expanded diameter section (17). The swinging member (15) is supported by a guide member (41) having an inner diameter surface formed into a continuous concave spherical surface.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、医薬品、食品業界をはじめ、粒子の加工処理(造粒、コーティング 等)を必要とする産業界で広く用いられる粒子加工装置において、処理容器内に 粒子加工用の処理液(バインダー液、コーティング液等)を供給するための処理 液供給装置に関するものである。 INDUSTRIAL APPLICABILITY The present invention is a particle processing apparatus widely used in the pharmaceutical industry, the food industry, and other industries that require particle processing (granulation, coating, etc.). , Coating liquid, etc.).

【0002】[0002]

【従来の技術】[Prior art]

粉粒体の造粒・コーティングを行なうための装置として、従来から流動層装置 が広く用いられている。この流動層装置では、処理容器の下部に多孔板や金網等 の通気性部材が配置されると共に、上部に粉粒体の飛散防止用の濾布が配置され ている。この処理容器の下部から空気流を噴出させたり、回転体・攪拌羽根を回 転させることにより、処理容器内の粉粒体を懸濁状態に浮揚流動させて流動層を 形成し、これに結合液やコーティング液を噴霧し、さらに必要に応じて粉体を供 給することにより所望の粒子加工が行なわれる。 A fluidized bed apparatus has been widely used as an apparatus for granulating and coating powder particles. In this fluidized bed apparatus, a breathable member such as a perforated plate or a wire net is arranged at the lower part of the processing container, and a filter cloth for preventing scattering of powdery particles is arranged at the upper part. By ejecting an air flow from the lower part of this processing container or rotating a rotating body / stirring blade, the powder and granules in the processing container are levitated and suspended in a suspended state to form a fluidized bed, which is then bonded. A desired particle is processed by spraying a liquid or a coating liquid and further supplying a powder if necessary.

【0003】 この種の流動層装置において、結合液等を噴霧するスプレーノズルの固定方法 には、上部から下向きに液滴を噴霧するよう固定したトップスプレー法と、 底面から上向きに液滴を噴霧するよう固定したボトムスプレー法と、処理容器 の下部側面から中心に向けて液滴を噴霧するよう固定したサイドスプレー法とが ある。In a fluidized bed apparatus of this type, a spray nozzle for spraying a binding liquid or the like is fixed by a top spray method in which droplets are sprayed downward from the top, and a droplet is sprayed upward from the bottom. There is a bottom spray method that is fixed so that it is fixed, and a side spray method that is fixed so that droplets are sprayed from the lower side surface of the processing container toward the center.

【0004】[0004]

【考案が解決しようとする課題】[Problems to be solved by the device]

上述の各固定方法のうち、トップスプレー法及びボトムスプレー法では、スプ レーノズルと粉粒体との間に距離があるために、噴霧した液滴の一部が粉粒体と 接触する前に乾燥してロスとなったり、液滴の粘度が変化して十分な造粒あるい はコーティング効果が期待できないという問題がある。これに対し、サイドスプ レー法では、粉粒体の密度の高い下部側面からスプレーするため、上述のような 液滴の乾燥等の問題が生じにくい点で優れた固定方法と言えるが、噴霧した液滴 が十分に分散・霧化していない状態でノズル先端近傍の粉粒体と接触するため、 局所的に液滴が付着して粗大粒子が生成される要因となる場合が多かった。 Among the fixing methods described above, in the top spray method and the bottom spray method, since there is a distance between the spray nozzle and the granules, some of the sprayed droplets are dried before coming into contact with the granules. As a result, there is a problem that a loss occurs, or the viscosity of the droplet changes, and sufficient granulation or a coating effect cannot be expected. On the other hand, the side spray method is an excellent fixing method in that the above-mentioned problems such as drying of droplets are less likely to occur because the spray is performed from the lower side surface of the granular material, which has a high density. Since the droplets come into contact with the granular material in the vicinity of the nozzle tip in a state where they are not sufficiently dispersed and atomized, there are many cases in which the droplets locally adhere to form coarse particles.

【0005】 係る問題点は、特開平2−90957号公報や特開平4-145937号公報に開示されたス プレーノズルを用いることにより解決可能である。即ち、スプレーノズルの周囲 に二次空気流路を設け、かかる二次空気流路から空気流を噴出してノズル先端近 傍に粉粒体の密度の希薄なスプレーゾーンを形成するのである。このスプレーゾ ーンにより、ノズル先端部近傍での粉粒体と液滴の接触が阻止されるので、十分 に分散・霧化された液滴を粉粒体と接触させることが可能となる。This problem can be solved by using the spray nozzle disclosed in Japanese Patent Application Laid-Open Nos. 2-90957 and 4-145937. That is, a secondary air flow passage is provided around the spray nozzle, and an air flow is ejected from the secondary air flow passage to form a spray zone near the tip of the nozzle in which the density of powder particles is low. This spray zone prevents contact between the particles and the droplets in the vicinity of the tip of the nozzle, so that the droplets that have been sufficiently dispersed and atomized can be brought into contact with the particles.

【0006】 しかし、特開平2−90957号のスプレーノズルでは、ノズルの先端部がこれを支 持する支持体よりも処理容器の内部方向に位置している。このため、ノズル先端 部から粉粒体と液滴の接触領域までの距離が相対的に短くなり、液滴が十分に分 散・霧化されないうちに粉粒体と接触するおそれがある。また、二次空気流路の 先端部が、ノズル先端部の形状に合わせて絞り込まれているため、スプレーゾー ンの形成領域が狭くなり、当該スプレーゾーンによる接触阻止機能が低下するお それもある。However, in the spray nozzle of Japanese Patent Application Laid-Open No. 2-90957, the tip of the nozzle is located inward of the processing container rather than the support that supports the nozzle. Therefore, the distance from the tip of the nozzle to the contact area between the powder and granules and the liquid droplet is relatively short, and the liquid droplet may come into contact with the powder or granular material before being sufficiently dispersed and atomized. In addition, since the tip of the secondary air flow path is narrowed down according to the shape of the nozzle tip, the spray zone formation area becomes narrower, which may reduce the contact blocking function of the spray zone. .

【0007】 一方、特開平4-145937号のスプレーノズルでは、上述のものと同様にスプレー ゾーンの形成領域が狭いという欠点がある。また、液滴の最適なスプレー位置は 、粉粒体の仕込量、粒子径、比重等により変化するが、スプレーノズルが処理容 器に固定されているため、処理粒子の変更毎にスプレーノズルの取り付け位置を 変更しなければならず、煩雑な交換作業が必要となる。On the other hand, the spray nozzle disclosed in Japanese Patent Laid-Open No. 4-145937 has a drawback that the area where the spray zone is formed is narrow as in the case of the above. Also, the optimum spray position of the liquid droplets varies depending on the amount of powder particles charged, the particle size, the specific gravity, etc. Since the mounting position must be changed, complicated replacement work is required.

【0008】 そこで、本考案は、液滴の噴霧方向を任意に選択できると共に、スプレーゾー ンの形成領域を広く確保でき且つ液滴を十分に分散霧化させ得る粒子加工装置の 処理液供給装置の提供を目的とする。Therefore, the present invention provides a treatment liquid supply device of a particle processing device capable of arbitrarily selecting the spraying direction of droplets, ensuring a wide spray zone forming region, and sufficiently dispersing and atomizing the droplets. For the purpose of providing.

【0009】[0009]

【課題を解決するための手段】[Means for Solving the Problems]

上記目的の達成のため、本考案装置は、処理容器内に収容された粉粒体に造粒 、コーティング等の加工処理を施す粒子加工装置の処理液供給装置であって、 処理容器の内部空間と連通する貫通孔を有し、前記貫通孔の処理容器側の端部 に末広がりの拡径部が形成された球体状の揺動部材と、 処理容器に固定され、内径面で前記揺動部材の外表面を摺動案内する案内部材 と、 前記揺動部材の貫通孔内に、噴射口を拡径部の開口より後退させて収納され、 前記噴射口よりバインダー液、コーティング液等の処理液を噴霧するスプレーノ ズルと、 前記スプレーノズルと揺動部材の内径面との間に設けられ、一端部が気体供給 源に連結されると共に、他端部が前記拡径部に連通された二次気体流路と を備えている。 In order to achieve the above-mentioned object, the device of the present invention is a processing liquid supply device of a particle processing device that performs processing such as granulation and coating on powder particles contained in the processing container, and is an internal space of the processing container. A spherical swing member having a through hole communicating with the through hole, and a diverging diameter expanding portion formed at the end of the through hole on the processing container side; and the swing member fixed to the processing container with an inner diameter surface. A guide member for slidingly guiding the outer surface of the injection member, and a treatment liquid such as a binder liquid or a coating liquid, which is accommodated in the through hole of the swing member by retracting the injection port from the opening of the expanded diameter portion. Is provided between the spray nozzle and the spray nozzle and the inner diameter surface of the oscillating member, one end of which is connected to the gas supply source and the other end of which is connected to the enlarged diameter part. And a secondary gas flow path.

【0010】 また、二次気体流路に、粉末供給口を設けた。Further, a powder supply port is provided in the secondary gas flow path.

【0011】 さらに、揺動部材及びスプレーノズルを分解可能に構成した。Further, the swing member and the spray nozzle are configured to be disassembled.

【0012】[0012]

【作用】[Action]

二次気体流路から拡径部内に導入された二次気体流は、拡径部に案内されてス プレーノズルの噴射口前方の広い空間にスプレーゾーンを形成する。このスプレ ーゾーンにより、ノズル先端部近傍での液滴と粉粒体の早期接触がより広い範囲 で阻止される。また、スプレーノズルの噴射口を拡径部の開口より後退させてい るので、噴射口から粉粒体と液滴の接触領域までの距離が大きくなる。さらに、 揺動部材は球体状をなしており、その外表面は案内部材の内径面で摺動案内され る。従って、揺動部材を上下左右の任意方向に揺動させることが可能となる。 The secondary gas flow introduced from the secondary gas passage into the expanded diameter portion is guided by the expanded diameter portion to form a spray zone in a wide space in front of the spray nozzle injection port. This spray zone prevents a wider range of early contact between the droplet and the granular material near the nozzle tip. Further, since the injection port of the spray nozzle is set back from the opening of the expanded diameter portion, the distance from the injection port to the contact area between the powder and granules and the droplet becomes large. Further, the rocking member has a spherical shape, and the outer surface thereof is slidably guided by the inner diameter surface of the guide member. Therefore, the swinging member can be swung in any direction up, down, left or right.

【0013】 また、二次気体流路に、粉末供給口を設けることにより、二次気体流路内に流 入した粉末は、二次空気流と共に拡径部から処理容器の内部空間に向けて吹き出 される。Further, by providing the powder supply port in the secondary gas flow passage, the powder flowing into the secondary gas flow passage is directed from the expanded diameter portion toward the internal space of the processing container together with the secondary air flow. Blown out.

【0014】[0014]

【実施例】【Example】

以下、本考案を、粒子加工装置の一つである転動流動層造粒装置に適用した場 合の実施例を図1乃至図4に基づいて説明する。 An embodiment in which the present invention is applied to a rolling fluidized bed granulating apparatus which is one of particle processing apparatuses will be described below with reference to FIGS. 1 to 4.

【0015】 図1は、転動流動層造粒装置の全体構造を示す縦断面図である。以下、この装 置の概略構造を説明する。FIG. 1 is a vertical cross-sectional view showing the entire structure of a rolling fluidized bed granulator. The schematic structure of this device will be described below.

【0016】 円筒状の処理容器(1)の底部には、中央に開口(2a)を有する底板(2)が 固定され、この底板(2)の開口(2a)には、円錐台状の通気部材(3)が装着 されている。この通気部材(3)は、多孔板や金網その他適当な通気性材料で構 成される。前記通気部材(3)の中心部には、中空の支柱(4)が立設され、こ の支柱(4)内に駆動源(図示省略)と連結した枢軸(6)が回転自在に収納さ れている。枢軸(6)の頂部には、ナット等の締結手段で回転体(7)が装着さ れる。この回転体(7)は、末広がりの傾斜壁を備えた截頭円錐台状をなし、傾 斜壁の下部には放射状に延びる複数枚の攪拌羽根(9)が、その先端を処理容器 (1)の側面壁(1a)に近接させると共に処理容器の底板から僅かに離隔させて 装着される。前記通気部材(3)の下方には、空気供給源(図示省略)と連結し た空気流路(10)が設けられている。A bottom plate (2) having an opening (2a) in the center is fixed to the bottom of the cylindrical processing container (1), and a frustoconical ventilation is provided in the opening (2a) of the bottom plate (2). The member (3) is fitted. This ventilation member (3) is made of a perforated plate, a wire mesh or other suitable air-permeable material. A hollow column (4) is erected in the center of the ventilation member (3), and a pivot (6) connected to a drive source (not shown) is rotatably housed in the column (4). Has been. The rotating body (7) is mounted on the top of the pivot (6) by fastening means such as a nut. This rotating body (7) is in the shape of a truncated cone with a sloping wall that widens toward the end, and a plurality of radially extending stirring blades (9) are provided at the bottom of the sloping wall at the tip of the processing container (1). ) Is installed close to the side wall (1a) and is slightly separated from the bottom plate of the processing container. Below the ventilation member (3), an air flow path (10) connected to an air supply source (not shown) is provided.

【0017】 空気供給源から供給された空気は、空気流路(10)を経て通気部材(3)を通 過し、回転体(7)の内部空間に流入する。そして、回転体(7)の裾先端部と 処理容器(1)の底板(2)との間隙より処理容器(1)の内部空間に噴出する 。この空気流と回転体(7)の回転動作との協働により、処理容器(1)の内部 空間に収容された粒子が旋回しながら吹き上げられて浮遊流動し、転動流動層を 形成する。噴出した空気流は処理容器(1)の上部に設けた排気口(11)から排 出される。この時、空気流中に混在する粉粒体が濾布(12)で回収される。The air supplied from the air supply source passes through the air passage (10), the ventilation member (3), and flows into the internal space of the rotating body (7). Then, it spouts into the internal space of the processing container (1) from the gap between the bottom end of the rotator (7) and the bottom plate (2) of the processing container (1). Due to the cooperation of this air flow and the rotating operation of the rotating body (7), the particles contained in the internal space of the processing container (1) are swirled up while floating and flowing to form a rolling fluidized bed. The jetted air flow is discharged from an exhaust port (11) provided in the upper part of the processing container (1). At this time, the granular material mixed in the air flow is collected by the filter cloth (12).

【0018】 本考案に係る処理液供給装置(13)は、処理容器(1)の側面壁(1a)に設け られる。この処理液供給装置(13)から上述の転動流動層中に処理液(結合液や コーティング液等)を供給することにより、目的とする粉粒体の加工処理、即ち 造粒やコーティングを行なうことが可能になる。以下、この処理液供給装置(13 )の構造を図2に基づいて説明する。The treatment liquid supply device (13) according to the present invention is provided on the side wall (1a) of the treatment container (1). By supplying the processing liquid (binding liquid, coating liquid, etc.) from the processing liquid supply device (13) into the tumbling fluidized bed, the target powder or granular material is processed, that is, granulated or coated. It will be possible. The structure of the treatment liquid supply device (13) will be described below with reference to FIG.

【0019】 球体状をなす揺動部材(15)には、一端部を末広がりに拡径させた貫通孔(16 )が形成される(以下、この末広がり部分を拡径部(17)と称する)。この貫通 孔(16)内には、筒状の外方部材(18)及び内方部材(19)を同心配置してなる スプレーノズル(20)が、揺動部材(15)の内径面との間に環状隙間を設け、且 つ、噴射口(21)を拡径部(17)の開口(17a)より後退させて収納される。前 記外方部材(18)は、分解可能のハメアイにより嵌合固定した外筒(22)と外側 ノズルキャップ(23)とで構成されている。また、内方部材(19)も、外方部材 (18)と同様に、分解可能のハメアイにより嵌合固定した内筒(25)と内側ノズ ルインサート(26)とで構成される。前記内側ノズルインサート(26)には、外 側ノズルキャップ(23)の内径面と接触する環状突起(27)が一体形成され、こ の環状突起(27)の外周面には、図3に示すように、複数の螺旋溝(28)が形成 される。The swing member (15) having a spherical shape is formed with a through hole (16) whose one end is expanded in diameter toward the end (hereinafter, this expanded end portion is referred to as an expanded diameter part (17)). . Inside the through hole (16), a spray nozzle (20) in which a tubular outer member (18) and a tubular outer member (19) are concentrically arranged is provided with the inner diameter surface of the rocking member (15). An annular gap is provided therebetween, and the injection port (21) is retracted from the opening (17a) of the expanded diameter portion (17) and stored. The outer member (18) is composed of an outer cylinder (22) fitted and fixed by a disassembleable hook and an outer nozzle cap (23). Further, the inner member (19) is also composed of an inner cylinder (25) and an inner nozzle insert (26) fitted and fixed by a disassembleable hook eye, like the outer member (18). The inner nozzle insert (26) is integrally formed with an annular protrusion (27) that comes into contact with the inner diameter surface of the outer nozzle cap (23), and the outer peripheral surface of this annular protrusion (27) is shown in FIG. Thus, a plurality of spiral grooves (28) are formed.

【0020】 前記外筒(22)の基端部は、ノズル支持部材(30)の一端面に設けた一次空気 流入口(31)に分解可能のハメアイにより嵌合固定される。また、内筒(25)の 基端部は、前記一次空気流入口(31)の対向位置に設けられた処理液供給口(32 )に上記ハメアイにより嵌合固定される。前記一次空気流入口(31)及び処理液 供給口(32)は、それぞれ空気供給源及び処理液供給源(何れも図示省略)に接 続される。A base end portion of the outer cylinder (22) is fitted and fixed to a primary air inlet (31) provided on one end surface of the nozzle support member (30) by a disassembleable hook eye. Further, the base end portion of the inner cylinder (25) is fitted and fixed to the processing liquid supply port (32) provided at the position facing the primary air inlet port (31) by the above-mentioned clasp eye. The primary air inlet (31) and the processing liquid supply port (32) are connected to an air supply source and a processing liquid supply source (neither shown).

【0021】 揺動部材(15)とノズル支持部材(30)との間には、ねじ等の締結手段(図示 省略)により筒状の中間部材(34)が装着される。この中間部材(34)の内部に は、当該中間部材(34)の内径面との間に環状隙間を設けてスプレーノズル(20 )の基端部が収納される。また、中間部材(34)には、前記環状隙間と連通する 二次気体供給口(35)が設けられる。この二次気体供給口(35)から圧縮ガス、 たとえば圧縮空気(二次空気)を供給すると、当該二次空気は中間部材(34)の 内径面の環状隙間、揺動部材(15)の内径面の環状隙間を順次通過して拡径部( 17)内に噴出する。以下の説明では、この二次空気の流路、即ち中間部材(34) 及び揺動部材(15)の内径面に形成された環状隙間を二次気体流路(36)と称す ることとする。A tubular intermediate member (34) is mounted between the swinging member (15) and the nozzle supporting member (30) by fastening means (not shown) such as a screw. Inside the intermediate member (34), the base end portion of the spray nozzle (20) is housed with an annular gap provided between the intermediate member (34) and the inner diameter surface of the intermediate member (34). Further, the intermediate member (34) is provided with a secondary gas supply port (35) communicating with the annular gap. When compressed gas, such as compressed air (secondary air), is supplied from this secondary gas supply port (35), the secondary air is generated in the annular gap of the inner diameter surface of the intermediate member (34) and the inner diameter of the rocking member (15). It sequentially passes through the annular gap in the surface and jets into the expanded diameter portion (17). In the following description, the flow path of the secondary air, that is, the annular gap formed on the inner diameter surfaces of the intermediate member (34) and the swing member (15) will be referred to as the secondary gas flow path (36). .

【0022】 前記揺動部材(15)は、その先端部を処理容器(1)の側面壁(1a)に設けた 開口部(38)に嵌め込んだ上で、側面壁(1a)に固設した内側案内部材(39)と 、この内側案内部材(39)にねじ等の締結手段で取り付けた外側案内部材(40) とからなる案内部材(41)により支持される。前記内側及び外側案内部材(39) (40)の分離面は、揺動部材(15)の最大外径部を通る位置に設けられている。 また、内側及び外側案内部材(39)(40)の内径面は、揺動部材(15)の外表面 と面接触可能の連続凹状球面に形成されている。この構成により、揺動部材(15 )の外表面が両案内部材(39)(40)の内径面で案内されるため、揺動部材(15 )、中間部材(34)及びノズル支持部材(30)が上下左右方向に一体的に揺動自 在となる。The swing member (15) has its tip end fitted into the opening (38) provided in the side wall (1a) of the processing container (1), and then fixed to the side wall (1a). The inner guide member (39) and the outer guide member (40) attached to the inner guide member (39) by fastening means such as screws are supported by the guide member (41). The separation surface of the inner and outer guide members (39) (40) is provided at a position passing through the maximum outer diameter portion of the swinging member (15). The inner diameter surfaces of the inner and outer guide members (39) (40) are formed as continuous concave spherical surfaces capable of making surface contact with the outer surface of the swing member (15). With this configuration, the outer surface of the swing member (15) is guided by the inner diameter surfaces of the guide members (39) (40), so that the swing member (15), the intermediate member (34), and the nozzle support member (30). ) Becomes a swinging movement integrally in the vertical and horizontal directions.

【0023】 本考案装置は、以上の構成からなる。以下、本考案装置の作用・効果を説明す る。The device of the present invention has the above configuration. The operation and effect of the device of the present invention will be described below.

【0024】 処理液供給源から供給された処理液は、処理液供給口(32)から内筒(25)に 流入し、内側ノズルインサート(26)の先端部から噴射される。一方、空気供給 源から供給された一次空気は、一次空気流入口(31)から外筒(22)と内筒(25 )の間の隙間に流入し、環状突起(27)の螺旋溝(28)を通過して旋回流となり 、前記内側ノズルインサート(26)から噴射された液滴に作用してこれを霧化す る。ここで、二次気体流路(36)から拡径部(17)内に二次空気流を噴出させる と、噴射口(21)の前方に粉粒体(43)の密度の低い空間(S)(以下、スプレ ーゾーンと称す)が形成される。The processing liquid supplied from the processing liquid supply source flows into the inner cylinder (25) from the processing liquid supply port (32) and is ejected from the tip of the inner nozzle insert (26). On the other hand, the primary air supplied from the air supply source flows into the gap between the outer cylinder (22) and the inner cylinder (25) from the primary air inlet (31), and the spiral groove (28) of the annular protrusion (27). ) And becomes a swirl flow, which acts on the droplets ejected from the inner nozzle insert (26) to atomize them. Here, when the secondary air flow is ejected from the secondary gas flow path (36) into the expanded diameter portion (17), the space (S) having a low density of the granular material (43) in front of the injection port (21) (S ) (Hereinafter referred to as a spray zone) is formed.

【0025】 このようなスプレーゾーン(S)の形成により、スプレーノズル(20)の噴射 口(21)近傍での液滴(44)と粉粒体(43)の接触が阻止される。即ち、液滴( 44)と粉粒体(43)の接触領域が噴射口(21)近傍から処理容器(1)の内部方 向に移行する。これにより、十分に分散・霧化させた液滴(44)を粉粒体(43) に接触させることができるようになる。By forming such a spray zone (S), contact between the liquid droplets (44) and the granular material (43) in the vicinity of the injection port (21) of the spray nozzle (20) is prevented. In other words, the contact area between the droplet (44) and the granular material (43) moves from the vicinity of the injection port (21) toward the inside of the processing container (1). As a result, the droplets (44) that have been sufficiently dispersed and atomized can be brought into contact with the granular material (43).

【0026】 本考案によれば、以下のような特有の効果を発揮することができる。According to the present invention, the following unique effects can be exhibited.

【0027】 二次空気流が末広がりの拡径部(17)に導入されるため、スプレーゾーン( S)の形成領域が従来品(特開平2−90957号及び特開平4-145937号)に比べて広 く確保される。これにより、液滴(44)と粉粒体(43)の早期接触がより広い範 囲で阻止され、粗大粒子の生成をより確実に防止することが可能となる。Since the secondary air flow is introduced into the radially expanded portion (17) that spreads toward the end, the area where the spray zone (S) is formed is smaller than that of the conventional products (JP-A-2-90957 and JP-A-4-145937). Widely secured. As a result, early contact between the droplet (44) and the granular material (43) is prevented in a wider range, and it becomes possible to more reliably prevent the generation of coarse particles.

【0028】 スプレーノズル(20)の噴射口(21)が拡径部(17)の開口(17a)より後 退した位置に設けられているので、噴射口(21)から接触領域までの距離を大き く確保できる。従って、液滴を十分に分散・霧化させることが可能となる。Since the injection port (21) of the spray nozzle (20) is provided at a position retracted from the opening (17a) of the expanded diameter part (17), the distance from the injection port (21) to the contact area can be reduced. It can be secured large. Therefore, it becomes possible to sufficiently disperse and atomize the droplets.

【0029】 上下左右の任意方向に処理液を噴霧できるので、粉粒体(43)の仕込量・粒 子径、比重等に適合したスプレー位置が自由に選択できる。Since the treatment liquid can be sprayed in any direction of up, down, left and right, it is possible to freely select a spray position suitable for the charging amount, particle diameter, specific gravity and the like of the powdery particles (43).

【0030】 ねじを緩めて外側案内部材(40)を内側案内部材(39)から取り外すことに より揺動部材(15)、ノズル支持部材(30)、中間部材(34)、スプレーノズル (20)といった装置の主要部を処理容器(1)から簡単に取り外すことができる 。しかも、この主要部は、それぞれの要素(揺動部材(15)、ノズル支持部材( 30)、中間部材(34)、スプレーノズル(20))毎に簡単に分解することができ 、スプレーノズル(20)も内筒(25)、内側ノズルインサート(26)、外筒(22 )、外側ノズルキャップ(23)に分解することができる。このように各構成要素 毎に完全分解できるので、洗浄等のメンテナンス作業が容易に且つ確実に行なえ るようになる。By loosening the screw and removing the outer guide member (40) from the inner guide member (39), the swing member (15), the nozzle support member (30), the intermediate member (34), and the spray nozzle (20). The main part of the device can be easily removed from the processing container (1). Moreover, this main part can be easily disassembled into the respective elements (the swinging member (15), the nozzle supporting member (30), the intermediate member (34), and the spray nozzle (20)). 20) can also be disassembled into an inner cylinder (25), an inner nozzle insert (26), an outer cylinder (22) and an outer nozzle cap (23). In this way, since each component can be completely disassembled, maintenance work such as cleaning can be performed easily and surely.

【0031】 処理容器(1)の側面壁(1a)から突出する揺動部材(15)が球状であるた め、揺動部材(15)上に落下した粉粒体は、当該揺動部材(15)の外表面に滞留 ・付着することなく円滑に滑り落ちる。従って、加工処理完了後の製品の回収率 及び品質を向上させることが可能となる。Since the oscillating member (15) protruding from the side wall (1a) of the processing container (1) is spherical, the powder or granules dropped on the oscillating member (15) will not be affected by the oscillating member (15). Stays on the outer surface of 15) ・ Slides off smoothly without adhering. Therefore, it is possible to improve the recovery rate and quality of the product after the processing is completed.

【0032】 図4に本考案装置の他の実施例を示す。これは、中間部材(34)に新たに粉末 供給用ホッパ(45)を装着すると共に、二次気体流路(36)に粉末供給口(46) を設けたもので、特に粉粒体の表面に層状の修飾造粒を施す場合に好適な装置で ある。粉末供給用ホッパ(45)に粉末を供給すると、この粉末が粉末供給口(46 )から二次気体流路(36)内に流入し、二次空気流と共に処理容器(1)の内部 空間に吹き出される。なお、同図では、二次気体供給口(35)の図示が省略され ている。FIG. 4 shows another embodiment of the device of the present invention. This is the one in which the powder supply hopper (45) is newly installed in the intermediate member (34) and the powder supply port (46) is provided in the secondary gas flow path (36), especially on the surface of the granular material. This is an apparatus suitable for performing layered modified granulation on. When the powder is supplied to the powder supply hopper (45), the powder flows into the secondary gas flow path (36) from the powder supply port (46) and enters the inner space of the processing container (1) together with the secondary air flow. Blown out. The secondary gas supply port (35) is not shown in the figure.

【0033】[0033]

【考案の効果】[Effect of device]

上述のように本考案装置によれば、二次空気流が末広がりの拡径部に導入され ているため、スプレーゾーンの形成領域が広く確保される。これにより、液滴と 粉粒体の早期接触がより広い範囲で阻止され、粗大粒子の生成をより確実に防止 することが可能となる。 As described above, according to the device of the present invention, since the secondary air flow is introduced into the radially expanded portion that is widened toward the end, a wide spray zone forming area is secured. As a result, early contact between the droplet and the granular material is blocked in a wider range, and it becomes possible to more reliably prevent the generation of coarse particles.

【0034】 また、スプレーノズルの噴射口を拡径部の開口より後退させているので、噴射 口から粉粒体と液滴とが接触する領域までの距離を大きく確保できる。従って、 液滴を十分に分散・霧化させることが可能となる。Further, since the injection port of the spray nozzle is set back from the opening of the expanded diameter portion, it is possible to secure a large distance from the injection port to the region where the powdery particles and the droplets come into contact with each other. Therefore, it becomes possible to sufficiently disperse and atomize the droplets.

【0035】 さらに、接線方向をはじめ、上下左右の任意方向に処理液を噴霧できるので、 粉粒体の仕込量・粒子径、比重等に適合したスプレー位置を自由に選択できるよ うになる。Furthermore, since the treatment liquid can be sprayed in any direction, including the tangential direction, up, down, left, and right, it becomes possible to freely select a spray position that suits the charged amount of powdered particles, particle size, specific gravity, and the like.

【0036】 また、二次気体流路に粉末供給口を設けることにより、この粉末供給口に供給 された粉末は、二次気体流路を通り、末広がりの拡径部から処理容器内の広い範 囲に吹き出される。従って、粉粒体に対し、より一層効率的に修飾造粒を施すこ とが可能となる。Further, by providing the powder supply port in the secondary gas flow path, the powder supplied to the powder supply port passes through the secondary gas flow path and extends from the diverging portion of the end to a wide range within the processing container. It is blown out to the wall. Therefore, it becomes possible to more efficiently perform the modified granulation on the granular material.

【0037】 さらに、揺動部材及びスプレーノズルを完全に分解可能とすることにより、洗 浄等のメンテナンス作業が容易に且つ確実に行なえるようになる。Furthermore, by making the swinging member and the spray nozzle completely disassembled, maintenance work such as cleaning can be performed easily and surely.

【図面の簡単な説明】[Brief description of drawings]

【図1】本考案に係る処理液供給装置を具備した転動流
動層造粒装置の縦断面図である。
FIG. 1 is a vertical cross-sectional view of a tumbling fluidized bed granulator having a treatment liquid supply device according to the present invention.

【図2】図1中のA−A線における処理液供給装置の断面
図である。
FIG. 2 is a cross-sectional view of the processing liquid supply apparatus taken along the line AA in FIG.

【図3】内側ノズルインサート付近の拡大平面図
(a)、及び、B−B線での断面図(b)である。
FIG. 3 is an enlarged plan view (a) near the inner nozzle insert and a cross-sectional view (b) taken along line BB.

【図4】本考案に係る処理液供給装置の他の実施例を示
す縦断面図である。
FIG. 4 is a vertical sectional view showing another embodiment of the processing liquid supply apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 処理容器 15 揺動部材 16 貫通孔 17 拡径部 21 開口 20 スプレーノズル 21 噴射口 36 二次気体流路 41 案内部材 1 Processing Container 15 Swing Member 16 Through Hole 17 Expanded Portion 21 Opening 20 Spray Nozzle 21 Injection Port 36 Secondary Gas Flow Path 41 Guide Member

Claims (3)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 処理容器内に収容された粉粒体に造粒、
コーティング等の加工処理を施す粒子加工装置の処理液
供給装置であって、 処理容器の内部空間と連通する貫通孔を有し、前記貫通
孔の処理容器側の端部に末広がりの拡径部が形成された
球体状の揺動部材と、 処理容器に固定され、内径面で前記揺動部材の外表面を
摺動案内する案内部材と、 前記揺動部材の貫通孔内に、噴射口を拡径部の開口より
後退させて収納され、前記噴射口よりバインダー液、コ
ーティング液等の処理液を噴霧するスプレーノズルと、 前記スプレーノズルと揺動部材の内径面との間に設けら
れ、一端部が気体供給源に連結されると共に、他端部が
前記拡径部に連通された二次気体流路とからなることを
特徴とする粒子加工装置の処理液供給装置。
1. Granulation into a granular material contained in a processing container,
A processing liquid supply device of a particle processing device for performing processing such as coating, which has a through hole communicating with the internal space of the processing container, and has a diverging expanded portion at the end of the through hole on the processing container side. The formed spherical rocking member, a guide member that is fixed to the processing container and slides and guides the outer surface of the rocking member by the inner diameter surface, and the injection port is expanded in the through hole of the rocking member. A spray nozzle that is retracted from the opening of the diameter portion and is sprayed with a treatment liquid such as a binder liquid and a coating liquid from the injection port, and is provided between the spray nozzle and the inner diameter surface of the swing member, and has one end portion. Is connected to a gas supply source, and the other end portion is composed of a secondary gas flow path communicating with the expanded diameter portion.
【請求項2】 前記二次気体流路に、粉末供給口を設け
たことを特徴とする請求項1記載の粒子加工装置の処理
液供給装置。
2. The treatment liquid supply apparatus for a particle processing apparatus according to claim 1, wherein a powder supply port is provided in the secondary gas flow path.
【請求項3】 前記揺動部材及びスプレーノズルが分解
可能に構成されたことを特徴とする請求項1記載の粒子
加工装置の処理液供給装置。
3. The treatment liquid supply apparatus for a particle processing apparatus according to claim 1, wherein the swing member and the spray nozzle are configured to be disassembled.
JP8878792U 1992-12-25 1992-12-25 Processing liquid supply device for particle processing equipment Withdrawn JPH0652929U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8878792U JPH0652929U (en) 1992-12-25 1992-12-25 Processing liquid supply device for particle processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8878792U JPH0652929U (en) 1992-12-25 1992-12-25 Processing liquid supply device for particle processing equipment

Publications (1)

Publication Number Publication Date
JPH0652929U true JPH0652929U (en) 1994-07-19

Family

ID=13952559

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8878792U Withdrawn JPH0652929U (en) 1992-12-25 1992-12-25 Processing liquid supply device for particle processing equipment

Country Status (1)

Country Link
JP (1) JPH0652929U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007160262A (en) * 2005-12-15 2007-06-28 Fuji Paudal Co Ltd Fluidized layer apparatus
CN114472887A (en) * 2021-12-30 2022-05-13 山东大学 Forming die and forming method for blade with multi-powder structure in circumferential direction

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007160262A (en) * 2005-12-15 2007-06-28 Fuji Paudal Co Ltd Fluidized layer apparatus
CN114472887A (en) * 2021-12-30 2022-05-13 山东大学 Forming die and forming method for blade with multi-powder structure in circumferential direction

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