JP7007759B2 - Sprayer, sprayer, and spray dryer - Google Patents

Sprayer, sprayer, and spray dryer Download PDF

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JP7007759B2
JP7007759B2 JP2020520951A JP2020520951A JP7007759B2 JP 7007759 B2 JP7007759 B2 JP 7007759B2 JP 2020520951 A JP2020520951 A JP 2020520951A JP 2020520951 A JP2020520951 A JP 2020520951A JP 7007759 B2 JP7007759 B2 JP 7007759B2
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spraying
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JPWO2019224967A1 (en
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晋介 加藤
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PRECI CO., LTD.
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B3/00Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements
    • B05B3/02Spraying or sprinkling apparatus with moving outlet elements or moving deflecting elements with rotating elements

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Description

本発明は、噴霧した溶液、スラリー等の原料液を乾燥することで乾燥粉体を製造する際に用いられる噴霧盤、当該噴霧盤を用いた噴霧装置、及び当該噴霧装置を用いた噴霧乾燥装置に関するものである。 The present invention is a spraying machine used for producing a dry powder by drying a sprayed solution, a raw material liquid such as a slurry, a spraying device using the spraying machine, and a spray drying device using the spraying device. It is about.

噴霧した溶液、スラリー等の原料液を、例えば、熱風により乾燥することで乾燥粉体(顆粒体)を製造する噴霧乾燥装置は、食料品、医薬品、金属材料、工業用材料等の製造分野において多用されている。一般的な噴霧乾燥装置は、少なくとも、溶液、スラリー等の原料液を噴霧する噴霧部と、噴霧した原料液に対して熱風等を接触させることにより、原料液に含まれる溶媒を蒸発させることで乾燥粉体を生成する乾燥部とを備える。 Spray-drying devices that produce dry powders (granule) by drying raw materials such as sprayed solutions and slurries with hot air are used in the fields of manufacturing foods, pharmaceuticals, metal materials, industrial materials, and the like. It is often used. A general spray-drying device evaporates the solvent contained in the raw material liquid by bringing hot air or the like into contact with the sprayed part that sprays the raw material liquid such as a solution or slurry at least. It is provided with a drying unit for producing a dry powder.

通常の並流型の噴霧乾燥装置においては、乾燥部天面の略中央部に噴霧部が設けられており、当該噴霧部で噴霧された原料液は高温ガス(例えば、熱風)との接触による溶媒の蒸発を伴いながら、乾燥部下部に自然落下し、乾燥粉体として回収される。このとき、粒径が小さく排気流に混入しやすい乾燥粉体は、排気手段に併設けられたサイクロン型集塵装置等により高温ガスの排気と併せて回収することもできる。 In a normal parallel flow type spray drying device, a spraying portion is provided in a substantially central portion of the top surface of the drying portion, and the raw material liquid sprayed by the spraying portion is in contact with a high temperature gas (for example, hot air). With the evaporation of the solvent, it naturally falls to the lower part of the dry part and is recovered as a dry powder. At this time, the dry powder having a small particle size and easily mixed in the exhaust flow can be recovered together with the exhaust of the high temperature gas by a cyclone type dust collector or the like provided together with the exhaust means.

噴霧部としては、回転ディスク、加圧ノズル、二流体ノズル等が用いられており、この中でも粘度分布がシャープな乾燥粉体が得られる、粒子径の制御が容易である等の理由から回転ディスクが選定されることが多い。回転ディスクには、ベーン型、ピン型、ケスナー(ベル)型といった各種ディスク形状が存在し、その使用用途・環境等に応じて適宜使い分けがなされている(例えば、特許文献1参照)。 A rotating disk, a pressurized nozzle, a two-fluid nozzle, or the like is used as the spraying part. Among them, a rotating disk is used because a dry powder having a sharp viscosity distribution can be obtained and the particle size can be easily controlled. Is often selected. There are various disc shapes such as vane type, pin type, and Kesner (bell) type for the rotating disc, and they are appropriately used according to the intended use, environment, and the like (see, for example, Patent Document 1).

特開2002-128570号公報Japanese Unexamined Patent Publication No. 2002-128570

回転ディスクは、一般に噴霧盤とも呼ばれ、この中でもピン型は円板(盤)形状を有する2枚の回転板が組み合わされた回転体として構成される。回転ディスクは、回転軸を介して伝達された駆動力により大凡1000~60000rpmの高速度で回転し、供給された溶液、スラリー等の原料液をその遠心力によって噴霧する。しかしながら、従来型の回転ディスクは、図12に例示する回転ディスク(噴霧盤900)のように、回転軸に対して水平方向である矢印A方向に原料液を噴霧するため、回転速度を低回転に制御し、大きい液滴を噴霧する条件や、原料液の比重が大きく、飛翔距離が長くなってしまう場合によっては、原料液の乾燥が不十分であるため、原料液が乾燥部内側側壁に未乾燥、半乾燥状態で接触し付着が多くなるため、乾燥粉体として回収することができず、収量が低下するといった問題があった。また、回転ディスクによる噴霧は、その回転速度がより高速となると、噴流が上側に広がり、原料液が乾燥部天面側に付着し収量が低下する、また、回転ディスクの上側回転板に原料液が付着することで回転ディスクの重量バランスが崩れ、適正な噴霧ができなくなり、最悪の場合噴霧装置が損傷するといった問題もあった。 The rotating disk is also generally called a spraying disk, and among them, the pin type is configured as a rotating body in which two rotating plates having a disk (disk) shape are combined. The rotating disk rotates at a high speed of about 1000 to 60,000 rpm by the driving force transmitted via the axis of rotation, and sprays the supplied raw material liquid such as a solution or slurry by the centrifugal force. However, the conventional rotary disk sprays the raw material liquid in the direction of arrow A, which is horizontal to the rotation axis, like the rotary disk (spraying machine 900) illustrated in FIG. 12, so that the rotation speed is low. In some cases, such as when large droplets are sprayed, the specific gravity of the raw material liquid is large, and the flight distance is long, the raw material liquid is not sufficiently dried, so the raw material liquid is applied to the inner side wall of the dried portion. Since it comes into contact with each other in an undried or semi-dried state and adheres to a large amount, it cannot be recovered as a dry powder, and there is a problem that the yield is lowered. Further, when the rotation speed of the spray by the rotating disk becomes higher, the jet flow spreads upward, the raw material liquid adheres to the top surface side of the dried portion, and the yield decreases, and the raw material liquid is applied to the upper rotating plate of the rotating disk. There is also a problem that the weight balance of the rotating disk is lost due to the adhesion, the proper spraying cannot be performed, and in the worst case, the spraying device is damaged.

また、本願発明者らの最近の研究により、回転ディスクは高速回転することで、回転ディスク内部へと向かう矢印B方向から回転ディスク外側(上側)へと向かう矢印C方向にかけての空気の流れが存在することが明らかとなっている。このような正規の噴霧方向に対して逆方向に作用する空気の流れは、回転ディスク内部における原料液の逆流、若しくは正規な原料液の流れを阻害する要因ともなりうることを示唆している。 Further, according to the recent research by the inventors of the present application, the rotating disk rotates at high speed, and there is an air flow from the arrow B direction toward the inside of the rotating disk to the arrow C direction toward the outside (upper side) of the rotating disk. It is clear that it will be done. It is suggested that such a flow of air acting in the direction opposite to the normal spraying direction may be a factor that hinders the backflow of the raw material liquid or the flow of the raw material liquid inside the rotating disk.

本発明はこのような実状に鑑みてなされたものであり、本発明の課題は、噴霧した原料液を乾燥部内側側壁に付着させることなく、鉛直下向き側の乾燥部下部方向に適切に導入することが可能な噴霧盤、当該噴霧盤を用いた噴霧装置、及び当該噴霧装置を用いた噴霧乾燥装置を提供することである。 The present invention has been made in view of such an actual situation, and the subject of the present invention is to appropriately introduce the sprayed raw material liquid toward the lower part of the dry portion on the vertically downward side without adhering to the inner side wall of the dry portion. It is an object of the present invention to provide a spraying machine capable of using the spraying machine, a spraying device using the spraying machine, and a spray drying device using the spraying device.

本願発明者は、上記課題を解決するため鋭意研究した結果、流体が近接する壁(面)に引き寄せられる、所謂、コアンダ効果を利用することにより、上記課題を解決することができることを見出し、本発明の完成に至った。 As a result of diligent research to solve the above-mentioned problems, the inventor of the present application has found that the above-mentioned problems can be solved by utilizing the so-called Coanda effect in which a fluid is attracted to an adjacent wall (surface). The invention was completed.

すなわち、本発明の第1の発明によれば、供給された原料液を所定の噴霧方向に噴霧する噴霧部材と、前記原料液の前記噴霧方向を鉛直下向き側に転向させる転向部材とを備え、前記噴霧部材は、中央部に開口部を有する上側回転板と、前記上側回転板と接続され、前記上側回転板に対して平行な平面を有する下側回転板とを含み、前記転向部材は、前記下側回転板の前記平面から鉛直下向き側に延在するエッジ部を有することを特徴とする噴霧盤が提供される。 That is, according to the first aspect of the present invention, a spray member for spraying the supplied raw material liquid in a predetermined spraying direction and a turning member for turning the spraying direction of the raw material liquid vertically downward are provided. The spray member includes an upper rotary plate having an opening in the center and a lower rotary plate connected to the upper rotary plate and having a plane parallel to the upper rotary plate . Provided is a spraying machine characterized by having an edge portion extending vertically downward from the plane of the lower rotating plate.

また、第1の発明においては、前記下側回転板は円板状に形成され、前記エッジ部は前記平面の外縁部から円環状に延在する傾斜面として形成されることを特徴とする噴霧盤を提供することができ、前記傾斜面は前記平面に対して5°~90°の傾斜を有することができる Further, in the first invention, the lower rotating plate is formed in a disk shape, and the edge portion is formed as an inclined surface extending in an annular shape from the outer edge portion of the plane. A board can be provided, the inclined surface can have an inclination of 5 ° to 90 ° with respect to the plane .

また、本発明の第2の発明によれば、供給された原料液を所定の噴霧方向に噴霧する噴霧部材と、前記原料液の前記噴霧方向を鉛直下向き側に転向させる転向部材とを有する噴霧盤と、前記噴霧盤に接続され、前記噴霧盤を所定の回転数で回転させる回転部とを備え、前記噴霧部材は、中央部に開口部を有する上側回転板と、前記上側回転板と接続され、前記上側回転板に対して平行な平面を有する下側回転板とを含み、前記転向部材は、前記下側回転板の前記平面から鉛直下向き側に延在するエッジ部を有することを特徴とする噴霧装置が提供される。 Further , according to the second aspect of the present invention, a spray having a spray member for spraying the supplied raw material liquid in a predetermined spray direction and a turning member for turning the spray direction of the raw material liquid vertically downward. The board is provided with a rotating portion connected to the spraying machine and rotating the spraying machine at a predetermined rotation speed, and the spraying member is connected to an upper rotating plate having an opening in a central portion and the upper rotating plate. The turning member includes an lower rotating plate having a plane parallel to the upper rotating plate, and the turning member has an edge portion extending vertically downward from the plane of the lower rotating plate. A spraying device is provided.

また、第2の発明においては、前記下側回転板は円板状に形成され、前記エッジ部は前記平面の外縁部から円環状に延在する傾斜面として形成されることを特徴とする噴霧装置を提供することができ、前記傾斜面は前記平面に対して5°~90°の傾斜を有することができる。Further, in the second invention, the lower rotating plate is formed in a disk shape, and the edge portion is formed as an inclined surface extending in an annular shape from the outer edge portion of the plane. The device can be provided and the inclined surface can have an inclination of 5 ° to 90 ° with respect to the plane.

また、本発明の第3の発明によれば、供給された原料液を所定の噴霧方向に噴霧する噴霧部材と、前記原料液の前記噴霧方向を鉛直下向き側に転向させる転向部材とを有する噴霧盤と、前記噴霧盤に接続され、前記噴霧盤を所定の回転数で回転させる回転部と、前記上側回転板の前記開口部を介して前記噴霧盤内部に原料液を供給する原料液供給部と、前記噴霧盤から噴霧された前記原料液を乾燥することによって乾燥粉体を生成する粉体生成部とを備え、前記噴霧部材は、中央部に開口部を有する上側回転板と、前記上側回転板と接続され、前記上側回転板に対して平行な平面を有する下側回転板とを含み、前記転向部材は、前記下側回転板の前記平面から鉛直下向き側に延在するエッジ部を有することを特徴とする噴霧乾燥装置を提供できる。 Further , according to the third aspect of the present invention, a spray having a spray member for spraying the supplied raw material liquid in a predetermined spray direction and a turning member for turning the spray direction of the raw material liquid vertically downward. A raw material liquid supply unit that is connected to the spraying machine, a rotating portion that rotates the spraying machine at a predetermined rotation speed, and a raw material liquid supply unit that supplies the raw material liquid to the inside of the spraying machine through the opening of the upper rotating plate. And a powder generating unit that produces dry powder by drying the raw material liquid sprayed from the spraying machine, the spray member includes an upper rotary plate having an opening in the center and the upper side. The turning member includes an lower rotating plate which is connected to the rotating plate and has a plane parallel to the upper rotating plate, and the turning member has an edge portion extending vertically downward from the plane of the lower rotating plate. It is possible to provide a spray drying device characterized by having .

また、本発明の第3の発明においては、前記下側回転板は円板状に形成され、前記エッジ部は前記平面の外縁部から円環状に延在する傾斜面として形成されることを特徴とする噴霧乾燥装置を提供することができ、前記傾斜面は前記平面に対して5°~90°の傾斜を有することができる。 Further, in the third aspect of the present invention, the lower rotating plate is formed in a disk shape, and the edge portion is formed as an inclined surface extending in an annular shape from the outer edge portion of the plane. The spray drying device can be provided, and the inclined surface can have an inclination of 5 ° to 90 ° with respect to the plane.

本発明によれば、噴霧した原料液を乾燥部内側側壁に付着させることなく、鉛直下向き側の乾燥部下部方向に適切に導入することが可能な噴霧盤、当該噴霧盤を用いた噴霧装置、及び当該噴霧装置を用いた噴霧乾燥装置を提供することができる。 According to the present invention, a spraying machine capable of appropriately introducing the sprayed raw material liquid toward the lower part of the drying part on the vertically downward side without adhering to the inner side wall of the drying part, a spraying device using the spraying machine, and the like. And a spray drying device using the spraying device can be provided.

本実施形態に係る噴霧乾燥装置50の装置構成を説明する概略構成図である。It is a schematic block diagram explaining the apparatus configuration of the spray drying apparatus 50 which concerns on this embodiment. 本実施形態に係る噴霧装置20の装置構成を説明する概略構成図である。It is a schematic block diagram explaining the apparatus configuration of the spraying apparatus 20 which concerns on this embodiment. 図2における本実施形態に係る噴霧盤10の拡大断面図である。FIG. 2 is an enlarged cross-sectional view of the spraying machine 10 according to the present embodiment in FIG. 本実施形態に係る噴霧盤10の平面図である。It is a top view of the spray board 10 which concerns on this embodiment. 試験で得られた乾燥粉体の粒度分布をグラフ化した図である。It is a figure which graphed the particle size distribution of the dry powder obtained in a test. 本発明に係る変形例を説明する図である。It is a figure explaining the modification which concerns on this invention. 本発明に係る変形例を説明する図である。It is a figure explaining the modification which concerns on this invention. 本発明に係る変形例を説明する図である。It is a figure explaining the modification which concerns on this invention. 本発明に係る変形例を説明する図である。It is a figure explaining the modification which concerns on this invention. 本発明に係る変形例を説明する図である。It is a figure explaining the modification which concerns on this invention. 本発明に係る変形例を説明する図である。It is a figure explaining the modification which concerns on this invention. 従来型の噴霧盤900を説明する図である。It is a figure explaining the conventional spraying machine 900.

以下、本発明の実施形態について図面を参照して説明する。なお、本発明は以下の記述に限定されるものではなく、本発明の要旨を逸脱しない範囲において適宜変更可能である。また、本発明の説明において、同一構成とすることができる部材については同一の符号を付してその説明を省略することがある。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. The present invention is not limited to the following description, and can be appropriately modified without departing from the gist of the present invention. Further, in the description of the present invention, the members having the same configuration may be designated by the same reference numerals and the description thereof may be omitted.

図1は、本実施形態に係る噴霧乾燥装置50の装置構成を説明する概略構成図である。本実施形態に係る噴霧乾燥装置50は、噴霧した溶液、スラリー等の原料液を乾燥することにより、微少粒子状の乾燥粉体を得ることが可能な装置である。このような噴霧乾燥装置50は、噴霧された原料液を乾燥することで乾燥粉体を生成する粉体生成部としての噴霧乾燥室500と、噴霧盤10を有し噴霧乾燥室500内部に原料液を噴霧する噴霧装置20と、噴霧装置20に原料液を供給する原料液供給部30と、噴霧乾燥室500内に高温ガスを供給する高温ガス供給部40と、噴霧乾燥室500下部に設けられ、当該噴霧乾燥室500内で乾燥した乾燥粉体を回収する第1乾燥粉体回収部502とを備える。 FIG. 1 is a schematic configuration diagram illustrating an apparatus configuration of the spray drying apparatus 50 according to the present embodiment. The spray drying device 50 according to the present embodiment is a device capable of obtaining a dry powder in the form of fine particles by drying a raw material liquid such as a sprayed solution or a slurry. Such a spray drying device 50 has a spray drying chamber 500 as a powder generating unit for producing dry powder by drying the sprayed raw material liquid, and a spraying board 10 and raw materials inside the spray drying chamber 500. A spray device 20 for spraying the liquid, a raw material liquid supply unit 30 for supplying the raw material liquid to the spray device 20, a high temperature gas supply unit 40 for supplying high temperature gas in the spray drying chamber 500, and a lower portion of the spray drying chamber 500 are provided. It is provided with a first dry powder recovery unit 502 for recovering the dry powder dried in the spray drying chamber 500.

噴霧乾燥室500は、噴霧装置20により噴霧された溶液、スラリー等の原料液を例えば、熱風といった高温ガスと接触させることにより乾燥を促すための容器である。噴霧乾燥室500は、例えばステンレス等の鋼材で形成することができ、下方に向かって円錐状に縮径する略円筒形状の中空体として形成することができる。高温ガスとの接触により乾燥して得られた乾燥粉体は、自重により噴霧乾燥室500下部に設けられた第1乾燥粉体回収部502において回収される。なお、第1乾燥粉体回収部502については、例えば、円錐形や四角錘形のホッパーや、トレイ、袋体といった種々の回収手段を適用することができ、ヘルール、バンド、クランプ、フランジ等の接続手段を介して噴霧乾燥室500と着脱自在に接続することが可能であれば、その種類、使用に制限はない。また、スクリューフィーダー、空気輸送等の何らかの手段によって乾燥粉体をサイロ等の貯蔵設備に輸送する形態としてもかまわない。 The spray drying chamber 500 is a container for promoting drying by contacting a raw material liquid such as a solution or slurry sprayed by the spray device 20 with a high temperature gas such as hot air. The spray drying chamber 500 can be formed of a steel material such as stainless steel, and can be formed as a substantially cylindrical hollow body whose diameter is reduced downward in a conical shape. The dry powder obtained by drying by contact with the high temperature gas is recovered by its own weight in the first dry powder recovery unit 502 provided in the lower part of the spray drying chamber 500. Various recovery means such as a conical or square pyramid-shaped hopper, a tray, and a bag can be applied to the first dry powder recovery unit 502, such as a ferrule, a band, a clamp, and a flange. As long as it can be detachably connected to the spray drying chamber 500 via the connecting means, there are no restrictions on its type and use. Further, the dry powder may be transported to a storage facility such as a silo by some means such as a screw feeder or air transport.

ところで、噴霧乾燥室500の外壁に衝撃、振動を与えることで乾燥室内側側壁、円錐部に堆積又は付着した乾燥粉体を強制流動させ、第1乾燥粉体回収部502に導く、ノッカー、バイブレータ等の衝撃・振動付与手段504を設けてもよい。また、エアーブルーム514、エアースイーパーといった気流により、壁面に堆積又は付着した乾燥粉体を払い落す手段を設けてもよい。さらに、噴霧乾燥室500内部に導入された高温ガスを排気するための排気管508にサイクロン型又はバグフィルタ型の集塵装置510を設けてもかまわない。これにより、粒径が小さく排気流に混入しやすい乾燥粉体を集塵装置510にて捕集し、第1乾燥粉体回収部502と同様に、集塵装置510に接続された第2乾燥粉体回収部512において回収することができる。また、第1乾燥粉体回収部502、第2乾燥粉体回収部512と2つ以上の捕集部を必ず設ける必要は無く、大部分の粉体の粒径が小さい、比重が低い等、噴霧乾燥室500下部の第1乾燥粉体回収部502に自重で落下しにくい粉体特性の場合は、第1乾燥粉体回収部502の設置箇所から排気管508を設けることにより、第2乾燥粉体回収部512で全ての粉体の回収を行う機構であっても構わない。 By the way, by applying impact and vibration to the outer wall of the spray drying chamber 500, the dry powder deposited or adhered to the side wall surface and the conical portion of the drying chamber is forcibly flowed and guided to the first dry powder recovery unit 502, a knocker and a vibrator. The impact / vibration applying means 504 such as the above may be provided. Further, a means for removing dry powder accumulated or adhering to the wall surface by an air flow such as an air bloom 514 or an air sweeper may be provided. Further, a cyclone type or bag filter type dust collector 510 may be provided in the exhaust pipe 508 for exhausting the high temperature gas introduced into the spray drying chamber 500. As a result, the dry powder having a small particle size and easily mixed in the exhaust stream is collected by the dust collector 510, and is connected to the dust collector 510 in the same manner as the first dry powder recovery unit 502. It can be recovered in the powder recovery section 512. Further, it is not always necessary to provide the first dry powder recovery unit 502, the second dry powder recovery unit 512, and two or more collection units, and most of the powder has a small particle size, a low specific gravity, and the like. In the case of powder characteristics that are difficult to drop due to its own weight in the first dry powder recovery unit 502 at the bottom of the spray drying chamber 500, the second drying is performed by providing an exhaust pipe 508 from the installation location of the first dry powder recovery unit 502. A mechanism may be used in which the powder recovery unit 512 recovers all the powder.

原料液供給部30は、原料液を収容する原料液タンク300と、ポンプ302とが原料液供給配管304により接続されている。原料液供給配管304は、噴霧装置20の原料液供給管200と接続されており、原料液タンク300に収容された原料液は、ポンプ302の駆動により噴霧装置20の噴霧盤10に供給される。なお、本発明に係る原料液としては、食料品、医薬品、金属材料、工業用材料等の分野における各種原料を用いることができるが、例えば、炭化ケイ素、窒化ケイ素、窒化アルミニウム、ジルコニア、アルミナ、ムライト、フェライト、フォルステライト、チタン酸バリウム、チタン酸ジルコン酸鉛、ステアタイト、ジルコンといった、所謂、ファインセラミックス原料、ガラス、セメント等のセラミックス原料等を適当な溶媒に分散することでスラリーとし、これを原料液として用いることができる。 In the raw material liquid supply unit 30, the raw material liquid tank 300 for accommodating the raw material liquid and the pump 302 are connected by a raw material liquid supply pipe 304. The raw material liquid supply pipe 304 is connected to the raw material liquid supply pipe 200 of the spraying device 20, and the raw material liquid contained in the raw material liquid tank 300 is supplied to the spraying board 10 of the spraying device 20 by driving the pump 302. .. As the raw material liquid according to the present invention, various raw materials in the fields of foodstuffs, pharmaceuticals, metal materials, industrial materials and the like can be used. For example, silicon carbide, silicon nitride, aluminum nitride, zirconia, alumina, etc. So-called fine ceramic raw materials such as mulite, ferrite, forsterite, barium titanate, lead titanate zirconate, steatite, and zircon, and ceramic raw materials such as glass and cement are dispersed in an appropriate solvent to form a slurry. Can be used as a raw material liquid.

高温ガス供給部40は、ガス発生装置400とガス供給配管402とにより構成されており、ガス発生装置400において発生した、例えば、熱風等の高温ガスを噴霧装置20の周辺に形成されたガス供給口404を介して噴霧乾燥室500内部に供給する。 The high temperature gas supply unit 40 is composed of a gas generator 400 and a gas supply pipe 402, and supplies high temperature gas such as hot air generated in the gas generator 400 around the spray device 20. It is supplied to the inside of the spray drying chamber 500 through the mouth 404.

図2は、本実施形態に係る噴霧装置20の装置構成を説明する概略構成図である。噴霧装置20は、噴霧盤10の高速回転に伴う遠心力により原料液を噴霧乾燥室500内部に噴霧する。噴霧装置20は、噴霧盤10に原料液を供給する原料液供給管200と、モータ202と、カップリング204を介してモータ202と接続され、モータ202の駆動に伴い回転する回転軸206と、図示せぬベアリング等を介し、鉛直方向下側に延在する回転軸206を軸支する上側軸支部208及び下側軸支部210とを備える。なお、回転軸206、原料液供給管200、上側軸支部208及び下側軸支部210はケーシング212に収納されており、ケーシング212上部には噴霧装置20全体を釣止するための取手214が設けられている。 FIG. 2 is a schematic configuration diagram illustrating an apparatus configuration of the spray apparatus 20 according to the present embodiment. The spraying device 20 sprays the raw material liquid into the spray drying chamber 500 by the centrifugal force accompanying the high-speed rotation of the spraying machine 10. The spraying device 20 includes a raw material liquid supply pipe 200 for supplying the raw material liquid to the spraying board 10, a motor 202, a rotating shaft 206 connected to the motor 202 via a coupling 204, and rotating with the drive of the motor 202. An upper shaft branch 208 and a lower shaft branch 210 that pivotally support the rotating shaft 206 extending downward in the vertical direction are provided via a bearing (not shown) or the like. The rotary shaft 206, the raw material liquid supply pipe 200, the upper shaft branch 208, and the lower shaft branch 210 are housed in the casing 212, and a handle 214 for stopping the entire spraying device 20 is provided on the upper part of the casing 212. Has been done.

上記構成を有する噴霧装置20は、噴霧乾燥室500の天面506略中央に設けられ、原料液供給配管304と接続された原料液供給管200を介して原料液を供給しながら、回転軸206先端に袋ナット216を介して取り付けられた噴霧盤10を高速回転させることにより、原料液を径方向外側(図中矢印X方向)に噴霧する。このとき、後述する噴霧盤10の下側回転板106は、平面部108から鉛直下向き側に延在するエッジ部116を有する構成であるため、図中矢印X方向に噴霧された原料液はコアンダ効果により、その噴流方向が鉛直下向き側の図中矢印Y方向に曲げられることになる。これにより、噴霧盤10から噴霧した液滴は、噴霧乾燥室500への到達距離が大幅に長くなることにより、十分な乾燥時間、距離が確保されるので、噴霧された原料液を噴霧乾燥室500の内側側壁に付着させることなく、適切に噴霧乾燥室500下部方向に導入することができる。噴霧方向が曲げられた原料液は、高温ガスとの接触により溶媒を蒸発させながら乾燥し、乾燥粉体としてその大部分が第1乾燥粉体回収部502において回収され、一部分は第2乾燥体回収部512において回収されることになる。 The spray device 20 having the above configuration is provided at substantially the center of the top surface 506 of the spray drying chamber 500, and supplies the raw material liquid through the raw material liquid supply pipe 200 connected to the raw material liquid supply pipe 304, while supplying the raw material liquid to the rotating shaft 206. By rotating the spraying machine 10 attached to the tip via the cap nut 216 at high speed, the raw material liquid is sprayed outward in the radial direction (in the direction of arrow X in the figure). At this time, since the lower rotary plate 106 of the spray plate 10 described later has an edge portion 116 extending vertically downward from the flat surface portion 108, the raw material liquid sprayed in the direction of arrow X in the figure is a Coanda. Due to the effect, the jet direction is bent in the direction of the arrow Y in the figure on the vertically downward side. As a result, the droplets sprayed from the spraying board 10 have a significantly longer reach to the spray drying chamber 500, so that a sufficient drying time and distance are secured. Therefore, the sprayed raw material liquid is sprayed into the spray drying chamber. It can be appropriately introduced toward the lower part of the spray drying chamber 500 without adhering to the inner side wall of the 500. The raw material liquid whose spray direction is bent is dried while evaporating the solvent by contact with the high temperature gas, and most of it is recovered as a dry powder in the first dry powder recovery unit 502, and a part of it is a second dry body. It will be collected in the collection unit 512.

次に、本実施形態に係る噴霧盤10の構成について図3及び図4を用いて説明する。図3は、噴霧盤10の拡大断面図であり、図4は噴霧盤10の平面図である。なお、本実施形態の説明
においては、円板(盤)形状を有する2枚の回転板がピンを介して組み合わされた回転体が高速回転することにより原料液を噴霧する所謂、ピン型を噴霧機構部として備えた噴霧部材について説明するものとする。
Next, the configuration of the spraying machine 10 according to the present embodiment will be described with reference to FIGS. 3 and 4. FIG. 3 is an enlarged cross-sectional view of the spraying machine 10, and FIG. 4 is a plan view of the spraying machine 10. In the description of the present embodiment, a so-called pin type is sprayed by spraying a raw material liquid by rotating a rotating body in which two rotating plates having a disk (disk) shape are combined via a pin at high speed. The spray member provided as a mechanical part shall be described.

噴霧盤10は、回転軸206に対して直交に取り付けた際に噴霧装置20側に位置する上側回転板100と、上側回転板100と平行に配され、複数のピン118によって上側回転板100と連結された下側回転板106とを備える。なお、下側回転板106の中央部分には、平面部108から立設するように回転軸接続部110が設けられており、その内部は回転軸206を挿通した状態で袋ナット216との螺合が可能となるようにナット部112が形成されている。すなわち、当該ナット部112において下側回転板106と回転軸206とを袋ナット216によって締結することにより、上側回転板100と下側回転板106とからなる回転体と回転軸206とが一体的に回転することになる。 The spray plate 10 is arranged in parallel with the upper rotary plate 100 located on the spray device 20 side when mounted orthogonally to the rotary shaft 206, and the upper rotary plate 100 by a plurality of pins 118. It is provided with a connected lower rotating plate 106. A rotating shaft connecting portion 110 is provided in the central portion of the lower rotating plate 106 so as to stand upright from the flat surface portion 108, and the inside thereof is screwed with the cap nut 216 with the rotating shaft 206 inserted. The nut portion 112 is formed so as to enable fitting. That is, by fastening the lower rotating plate 106 and the rotating shaft 206 with the cap nut 216 in the nut portion 112, the rotating body composed of the upper rotating plate 100 and the lower rotating plate 106 and the rotating shaft 206 are integrated. Will rotate to.

上側回転板100は、中央部が開口部104となるように形成された円環部102を有する環状円板体として構成され、当該開口部104には、原料液供給管200が挿通される。ピン118は、金属ロッドとして構成され、図4に示すように、上側回転板100の円環部102の周縁部に沿って同心円状に等角度間隔で配置される。上側回転板100と下側回転板106を連結する場合には、上側回転板100と下側回転板106とのそれぞれの配置位置にピン118を配置後、皿ネジ120で螺合することにより上側回転板100と下側回転板106とを連結することができる。なお、図4では、ピン118を合計16本用いた例について示されているが、ピン118の本数はこれに限定されず、上側回転板100と下側回転板106とを連結し、回転中に緩みが発生するといった不具合が生じるものでなければ使用する本数に制限はない。 The upper rotary plate 100 is configured as an annular disk body having an annular portion 102 formed so that the central portion is an opening 104, and the raw material liquid supply pipe 200 is inserted through the opening 104. The pins 118 are configured as metal rods, and as shown in FIG. 4, are arranged concentrically at equal intervals along the peripheral edge of the annular portion 102 of the upper rotary plate 100. When connecting the upper rotary plate 100 and the lower rotary plate 106, the pins 118 are placed at the respective arrangement positions of the upper rotary plate 100 and the lower rotary plate 106, and then screwed with the countersunk screw 120 to be screwed on the upper side. The rotary plate 100 and the lower rotary plate 106 can be connected. Although FIG. 4 shows an example in which a total of 16 pins 118 are used, the number of pins 118 is not limited to this, and the upper rotating plate 100 and the lower rotating plate 106 are connected and rotating. There is no limit to the number of pieces that can be used unless there is a problem such as loosening.

下側回転板106は、上側回転板100の円環部102に対して平行な平面部108を有する円板体として構成され、当該平面部108の外縁部114から鉛直下向き側に延在する転向部材としてのエッジ部116を有する。すなわち、エッジ部116は、図3に示すように、平面部108の外縁部114全域に亘って円環状に張り出した傾斜面として形成されている。平面部108に対するエッジ部116の傾斜角度θ1として、図3では、θ1=45°の例を示しているが、当該傾斜角度は、原料液の粘度、比重や蒸気圧等、噴霧盤10の回転速度、熱風温度、高温ガス量等、噴霧装置本体と噴霧盤との距離等、各種条件によって最適な傾斜角度は様々であるため、5°~90°の範囲で適宜選択することが好ましい。なお、下側回転板106のエッジ部116先端を含めた外径S(本実施形態では111mm)は、上側回転板100の外径T(本実施形態では110mm)と略同じ長さとなるように構成されているが、これらの長さも適宜変更することが可能である。 The lower rotary plate 106 is configured as a disk body having a flat surface portion 108 parallel to the annular portion 102 of the upper rotary plate 100, and is rotated vertically downward from the outer edge portion 114 of the flat surface portion 108. It has an edge portion 116 as a member. That is, as shown in FIG. 3, the edge portion 116 is formed as an inclined surface that projects in an annular shape over the entire outer edge portion 114 of the flat surface portion 108. As the inclination angle θ1 of the edge portion 116 with respect to the flat surface portion 108, an example of θ1 = 45 ° is shown in FIG. Since the optimum tilt angle varies depending on various conditions such as speed, hot air temperature, amount of high-temperature gas, distance between the spraying device main body and the spraying board, it is preferable to appropriately select the tilt angle in the range of 5 ° to 90 °. The outer diameter S (111 mm in the present embodiment) including the tip of the edge portion 116 of the lower rotary plate 106 has substantially the same length as the outer diameter T (110 mm in the present embodiment) of the upper rotary plate 100. Although it is configured, these lengths can be changed as appropriate.

上記構成を有する噴霧盤10を用いて原料液を噴霧する場合には、上側回転体100の開口部104に挿通された原料液供給管200を介して噴霧盤10内部に原料液を供給した状態で噴霧盤10を大凡1000~60000rpmの速度で回転させる。噴霧盤10の回転に伴う遠心力によって、盤内部に供給された原料液は、図2中矢印X方向である、下側回転板106の平面部108から外縁部114方向に流れる。外縁部114に到達した噴流は、外縁部114から延在するエッジ部116によって、その噴流方向が図2中矢印Y方向である、鉛直下向き側方向に曲げられることになる。これにより、噴霧された原料液を噴霧乾燥室500の内側側壁最短の水平方向へ飛翔させることなく、十分な乾燥時間、距離が確保されるため、原料液を当該内側側壁に付着させることなく、適切に噴霧乾燥室500下部方向に導入することができる。噴霧方向が曲げられた原料液は、高温ガスとの接触により溶媒を蒸発させながら乾燥し、乾燥粉体としてその大部分が第1乾燥粉体回収部502において回収され、一部分は第2乾燥体回収部512において回収されることになる。 When the raw material liquid is sprayed using the spraying machine 10 having the above configuration, the raw material liquid is supplied to the inside of the spraying machine 10 through the raw material liquid supply pipe 200 inserted through the opening 104 of the upper rotating body 100. The atomizer 10 is rotated at a speed of about 1000 to 60,000 rpm. The raw material liquid supplied to the inside of the plate by the centrifugal force accompanying the rotation of the spray plate 10 flows from the flat surface portion 108 of the lower rotating plate 106 toward the outer edge portion 114, which is the direction of the arrow X in FIG. The jet that reaches the outer edge portion 114 is bent by the edge portion 116 extending from the outer edge portion 114 in the vertical downward side direction in which the jet direction is the Y direction of the arrow in FIG. As a result, a sufficient drying time and distance are secured without causing the sprayed raw material liquid to fly in the shortest horizontal direction on the inner side wall of the spray drying chamber 500, so that the raw material liquid does not adhere to the inner side wall. It can be appropriately introduced toward the lower part of the spray drying chamber 500. The raw material liquid whose spray direction is bent is dried while evaporating the solvent by contact with the high temperature gas, and most of it is recovered as a dry powder in the first dry powder recovery unit 502, and a part of it is a second dry body. It will be collected in the collection unit 512.

[実施例]
本実施形態に係る噴霧盤10による効果を確認するため、図12に示す従来型の噴霧盤900のそれぞれを本実施形態に係る噴霧乾燥装置50と略同構成の噴霧乾燥装置に装着し、溶液、スラリー等の原料液から乾燥粉末を得る試験を行った。
[Example]
In order to confirm the effect of the spraying machine 10 according to the present embodiment, each of the conventional spraying machines 900 shown in FIG. 12 is attached to a spray drying device having substantially the same configuration as the spray drying device 50 according to the present embodiment, and a solution is provided. , A test was conducted to obtain a dry powder from a raw material solution such as a slurry.

本試験は、表1に示す条件下で行うものとし、原料液としてデキストリン水溶液を用いた。なお、噴霧乾燥室500直下に設けた第1乾燥粉体回収部502及び集塵装置510の直下に設けた第2乾燥粉体回収部512において回収された乾燥粉体の合計収量から収率を算出するものとし、これと同時に得られた乾燥粉体の粒度分布も併せて測定した。 This test was carried out under the conditions shown in Table 1, and an aqueous dextrin solution was used as the raw material solution. The yield is calculated from the total yield of the dry powder recovered in the first dry powder recovery unit 502 provided directly under the spray drying chamber 500 and the second dry powder recovery unit 512 provided directly under the dust collector 510. It was calculated, and the particle size distribution of the obtained dry powder was also measured at the same time.

Figure 0007007759000001
Figure 0007007759000001

表1から明らかな様に、本実施形態に係る噴霧盤10を用いた場合、収率は86.7%であり、従来型の噴霧盤900を用いた場合の収率(69.4%)を大きく上回る結果が得られた。これは、前述したように、本実施形態に係る噴霧盤10を用いた場合、噴霧された原料液はコアンダ効果により、その噴流方向が鉛直下向き側に曲げられることになる。これにより、噴霧された原料液を噴霧乾燥室500の内側側壁に付着させることなく、適切に噴霧乾燥室500下部方向に導入することができたため、乾燥粉体の回収量が向上したためだと考えられる。 As is clear from Table 1, when the spraying machine 10 according to the present embodiment is used, the yield is 86.7%, and the yield when the conventional spraying machine 900 is used (69.4%). The result was much higher than that. This is because, as described above, when the spraying machine 10 according to the present embodiment is used, the jet direction of the sprayed raw material liquid is bent vertically downward due to the Coanda effect. As a result, the sprayed raw material liquid could be appropriately introduced toward the lower part of the spray drying chamber 500 without adhering to the inner side wall of the spray drying chamber 500, and it is considered that the recovery amount of the dried powder was improved. Be done.

図5は、今回の試験において得られた乾燥粉体の粒度分布をグラフ化した図である。本実施形態に係る噴霧盤10を用いた場合、図5の実線で示されるとおり、非常にシャープな形状の粒度分布が得られ、従来型の噴霧盤900を用いた場合に得られた乾燥粉体の累積50%粒径(72.8μm)よりも大きく82.9μmであった。噴霧盤10を用いた場合の粒度分布は噴霧盤900のそれと比較して、粒径が大きい値がシャープな形状のグラフとなっているため、大きい液滴が噴霧乾燥室500の下部方向へ導入され、内側側壁までに乾燥する十分な到達距離、時間が与えられたため、大きい粒子として第1乾燥粉体回収部502で回収され、高い収率となった。これに対して、噴霧盤900を用いた場合には、水平方向へ飛翔する噴霧液滴が多く、大きい液滴は充分な乾燥までに必要な距離、時間が与えられないまま内側側壁に到達して付着したため、収量が低く、累積50%粒径の値も小さくなったものと想定される。 FIG. 5 is a graph showing the particle size distribution of the dry powder obtained in this test. When the spraying machine 10 according to the present embodiment is used, as shown by the solid line in FIG. 5, a particle size distribution having a very sharp shape is obtained, and the dry powder obtained when the conventional spraying machine 900 is used. It was 82.9 μm, which was larger than the cumulative 50% particle size (72.8 μm) of the body. Since the particle size distribution when the spraying machine 10 is used is a graph in which the large particle size is sharper than that of the spraying machine 900, large droplets are introduced toward the lower part of the spray drying chamber 500. Then, since sufficient reach and time for drying to the inner side wall were given, the particles were recovered as large particles by the first dry powder recovery unit 502, and the yield was high. On the other hand, when the spray plate 900 is used, many spray droplets fly in the horizontal direction, and the large droplets reach the inner side wall without being given the necessary distance and time for sufficient drying. It is presumed that the yield was low and the cumulative 50% particle size was also small.

[変形例]
本発明の実施形態に係る噴霧盤の説明では、転向部材として所定の傾斜角度で傾斜したエッジ部116を転向部材として有する噴霧盤10について説明した。しかしながら、本発明に係る噴霧盤は上記構成に限定されるものではない。例えば、図6に示す噴霧盤60のように、下側回転板101の外縁部114全域に亘って円環状に張り出す転向部材としてのエッジ部103の傾斜片を第1傾斜片103a、第2傾斜片103b等のように二段、三段等の複数回に分けて傾斜させてもよい。この場合、第1傾斜片103aの傾斜角θ2、第2傾斜片103bの傾斜角θ3は同角度となるように構成してもよいが、傾斜角θ2>傾斜角θ3の関係、すなわち、鈍角から順に鋭角となるように構成することが好ましい。また、例えば、図7に示す噴霧盤70のように、下側回転板105の外縁部114全域に亘って円環状に張り出す転向部材としてのエッジ部107の傾斜片をその先端部分が鉛直下向きとなるように湾曲状に形成してもかまわない。
[Modification example]
In the description of the spraying machine according to the embodiment of the present invention, the spraying machine 10 having the edge portion 116 inclined at a predetermined inclination angle as the turning member as the turning member has been described. However, the spraying machine according to the present invention is not limited to the above configuration. For example, like the spraying machine 60 shown in FIG. 6, the inclined pieces of the edge portion 103 as the turning member projecting in an annular shape over the entire outer edge portion 114 of the lower rotating plate 101 are the first inclined pieces 103a and the second. Like the inclined piece 103b or the like, it may be inclined in a plurality of times such as two steps and three steps. In this case, the tilt angle θ2 of the first tilt piece 103a and the tilt angle θ3 of the second tilt piece 103b may be configured to be the same angle, but from the relationship of the tilt angle θ2> the tilt angle θ3, that is, from the obtuse angle. It is preferable to configure them so that they have sharp angles in order. Further, for example, as in the spray plate 70 shown in FIG. 7, the tip portion of the inclined piece of the edge portion 107 as a turning member projecting in an annular shape over the entire outer edge portion 114 of the lower rotating plate 105 is vertically downward. It may be formed in a curved shape so as to be.

また、本発明の実施形態に係る噴霧盤の説明では、下側回転板106のエッジ部116先端を含めた外径Sと、上側回転板100の外径Tとが略同じ長さとなるように構成された噴霧盤10について説明したが、これに限定されず、例えば、図8に示すように、下側回転板109のエッジ部111先端部分を含めた外径S’が上側回転板100の外径Tより大きく、換言すると、エッジ部111の傾斜片が噴霧盤10に係るエッジ部116の傾斜片の長さよりも長くなるよう構成することも可能である。転向部材としてのエッジ部111の傾斜片の長さを長くすることにより、コアンダ効果に伴う原料液の引付効果が増大し、原料液の噴流方向をより効率的に鉛直下向き側に転向させることが可能になると期待できる。 Further, in the description of the spraying machine according to the embodiment of the present invention, the outer diameter S including the tip of the edge portion 116 of the lower rotary plate 106 and the outer diameter T of the upper rotary plate 100 are substantially the same length. Although the configured spray plate 10 has been described, the present invention is not limited to this, and for example, as shown in FIG. 8, the outer diameter S'including the tip portion of the edge portion 111 of the lower rotary plate 109 is the upper rotary plate 100. It is also possible to configure the inclined piece of the edge portion 111 to be larger than the outer diameter T, in other words, to be longer than the length of the inclined piece of the edge portion 116 related to the spray plate 10. By increasing the length of the inclined piece of the edge portion 111 as the turning member, the attraction effect of the raw material liquid due to the Coanda effect is increased, and the jet direction of the raw material liquid is more efficiently turned to the vertically downward side. Can be expected to be possible.

さらに、図9に示す噴霧盤90のように、噴霧された原料液を衝突させることにより鉛直下向き側にガイドする衝突ガイド部115を、下側回転板106のエッジ部116と同様に所定の傾斜角を有する傾斜面として構成することも可能である。衝突ガイド部115は、上側回転板117の円環部102の外縁部113全域に亘って円環状に張り出した傾斜面として形成することができ、下側回転板106のエッジ部116によるコアンダ効果を阻害せぬよう、衝突ガイド部115の傾斜面は、当該エッジ部116よりも浅い傾斜角とするか、又は傾斜片をエッジ部116のそれよりも短くことが好ましい。これにより、下側回転板106のエッジ部116によるコアンダ効果を阻害することなく、効率よく原料液を下側回転板106側に導くことができる。 Further, like the spraying machine 90 shown in FIG. 9, the collision guide portion 115 that guides the sprayed raw material liquid to the vertically downward side by colliding with the sprayed raw material liquid has a predetermined inclination like the edge portion 116 of the lower rotating plate 106. It can also be configured as an inclined surface with corners. The collision guide portion 115 can be formed as an inclined surface that projects in an annular shape over the entire outer edge portion 113 of the annular portion 102 of the upper rotary plate 117, and the Coanda effect due to the edge portion 116 of the lower rotary plate 106 can be obtained. It is preferable that the inclined surface of the collision guide portion 115 has an inclination angle shallower than that of the edge portion 116, or the inclined piece is shorter than that of the edge portion 116 so as not to hinder the collision guide portion 115. As a result, the raw material liquid can be efficiently guided to the lower rotating plate 106 side without disturbing the Coanda effect due to the edge portion 116 of the lower rotating plate 106.

これまでの本発明の説明においては、ピン型の噴霧機構を備えた噴霧盤について説明したが、本発明はこれに限定されず、例えば、ケスナー型、ベーン型、及びスリットベーン型のそれぞれを噴霧機構とする噴霧盤に対して適用することも無論可能である。 In the description of the present invention so far, a spraying machine provided with a pin-type spraying mechanism has been described, but the present invention is not limited to this, and for example, each of the Kessner type, vane type, and slit vane type is sprayed. Of course, it is also possible to apply it to the spraying machine as a mechanism.

図10は、本発明を適用したケスナー型(a)、ベーン型(b)、スリットベーン型(c)の噴霧機構を備えた各噴霧盤の形態を説明する概略図である。なお、ここでの説明では理解を容易とするために、噴霧機構以外の部分を断面図として表している。 FIG. 10 is a schematic view illustrating a form of each spraying machine provided with a Kessner type (a), vane type (b), and slit vane type (c) spraying mechanism to which the present invention is applied. In the description here, for the sake of ease of understanding, the parts other than the spraying mechanism are shown as a cross-sectional view.

図10(a)に係る噴霧盤600は、逆椀状のケスナー型噴霧機構602に対し接続部606を介して回転板608が設けられ、当該回転板608の外縁部610から鉛直下向き側に延在する転向部材としてのエッジ部612が形成された噴霧盤である。エッジ部612は、回転板608の外縁部610全域に亘って円環状に張り出した傾斜面として形成されている。ケスナー型噴霧機構602の椀内壁604から噴霧された原料液は、外縁部610から延在するエッジ部612によって、その噴流方向が鉛直下向き側方向に曲げられることになる。これにより、噴霧された原料液は、十分な乾燥時間、距離が確保されるため、当該原料液を当該内側側壁に付着させることなく、適切に噴霧乾燥室500下部方向に導入することができる。 In the spraying machine 600 according to FIG. 10A, a rotating plate 608 is provided to the inverted bowl-shaped Kessner-type spraying mechanism 602 via a connecting portion 606, and extends vertically downward from the outer edge portion 610 of the rotating plate 608. It is a spraying machine on which an edge portion 612 as an existing turning member is formed. The edge portion 612 is formed as an inclined surface that projects in an annular shape over the entire outer edge portion 610 of the rotating plate 608. The raw material liquid sprayed from the bowl inner wall 604 of the Kessner-type spraying mechanism 602 is bent in the vertical downward direction by the edge portion 612 extending from the outer edge portion 610. As a result, the sprayed raw material liquid can be appropriately introduced toward the lower part of the spray drying chamber 500 without adhering the raw material liquid to the inner side wall because a sufficient drying time and a sufficient distance are secured.

図10(b)に係る噴霧盤620は、上側回転板626と下側回転板628とが噴霧口624を有する噴霧壁630によって連結されることにより形成された円盤状のベーン型噴霧機構622を備える。噴霧盤620は、下側回転板628の外縁部632から鉛直下向き側に延在する転向部材としてのエッジ部634を有する。エッジ部634は、下側回転板628の外縁部632全域に亘って円環状に張り出した傾斜面として形成されている。ベーン型噴霧機構622の噴霧口624から噴霧された原料液は、外縁部632から延在するエッジ部634によって、その噴流方向が鉛直下向き側方向に曲げられることになる。これにより、噴霧された原料液を噴霧乾燥室500の内側側壁最短の水平方向へ飛翔させることなく、十分な乾燥時間、距離が確保されるため、原料液を当該内側側壁に付着させることなく、適切に噴霧乾燥室500下部方向に導入することができる。 The spraying machine 620 according to FIG. 10B has a disk-shaped vane-shaped spraying mechanism 622 formed by connecting the upper rotating plate 626 and the lower rotating plate 628 by a spray wall 630 having a spray port 624. Be prepared. The spraying machine 620 has an edge portion 634 as a turning member extending vertically downward from the outer edge portion 632 of the lower rotating plate 628. The edge portion 634 is formed as an inclined surface that projects in an annular shape over the entire outer edge portion 632 of the lower rotating plate 628. The raw material liquid sprayed from the spray port 624 of the vane-type spray mechanism 622 is bent vertically downward by the edge portion 634 extending from the outer edge portion 632. As a result, a sufficient drying time and distance are secured without causing the sprayed raw material liquid to fly in the shortest horizontal direction on the inner side wall of the spray drying chamber 500, so that the raw material liquid does not adhere to the inner side wall. It can be appropriately introduced toward the lower part of the spray drying chamber 500.

図10(c)に係る噴霧盤640は、図10(b)で示した噴霧盤620と同様に、上側回転板646と下側回転板648とがスリット形状の噴霧口644を有する噴霧壁650によって連結されることにより形成された円盤状のスリットベーン型噴霧機構642を備える。噴霧盤640は下側回転板648の外縁部652から鉛直下向き側に延在する転向部材としてのエッジ部654を有する。エッジ部654は、下側回転板648の外縁部652全域に亘って円環状に張り出した傾斜面として形成されている。スリットベーン型噴霧機構642の噴霧口644から噴霧された原料液は、外縁部652から延在するエッジ部654によって、その噴流方向が鉛直下向き側方向に曲げられることになる。これにより、噴霧された原料液を噴霧乾燥室500の内側側壁最短の水平方向へ飛翔させることなく、十分な乾燥時間、距離が確保されるため、原料液を当該内側側壁に付着させることなく、適切に噴霧乾燥室500下部方向に導入することができる。 The spray plate 640 according to FIG. 10 (c) has a spray wall 650 in which the upper rotary plate 646 and the lower rotary plate 648 have a slit-shaped spray port 644, similarly to the spray plate 620 shown in FIG. 10 (b). It is provided with a disk-shaped slit vane type spray mechanism 642 formed by being connected by. The spraying machine 640 has an edge portion 654 as a turning member extending vertically downward from the outer edge portion 652 of the lower rotating plate 648. The edge portion 654 is formed as an inclined surface that projects in an annular shape over the entire outer edge portion 652 of the lower rotating plate 648. The raw material liquid sprayed from the spray port 644 of the slit vane type spray mechanism 642 is bent vertically downward by the edge portion 654 extending from the outer edge portion 652. As a result, a sufficient drying time and distance are secured without causing the sprayed raw material liquid to fly in the shortest horizontal direction on the inner side wall of the spray drying chamber 500, so that the raw material liquid does not adhere to the inner side wall. It can be appropriately introduced toward the lower part of the spray drying chamber 500.

また、例えば、前述したケスナー型噴霧機構を備えた噴霧盤において、上記で説明したエッジ部等を別途設けなくとも原料液の噴流方向を鉛直下向き側方向に転向させる形態も可能である。ここで、図11(a)は従来のケスナー型噴霧機構を備えた噴霧盤700の断面形状を説明する断面図であり、図11(b)は本発明を適用したケスナー型噴霧機構を備えた噴霧盤800の断面形状を説明する断面図である。 Further, for example, in the spraying machine provided with the above-mentioned Kesner type spraying mechanism, the jet direction of the raw material liquid can be turned vertically downward without separately providing the edge portion and the like described above. Here, FIG. 11A is a cross-sectional view illustrating a cross-sectional shape of a spraying machine 700 provided with a conventional Kesner-type spraying mechanism, and FIG. 11B is provided with a Kesner-type spraying mechanism to which the present invention is applied. It is sectional drawing explaining the sectional shape of the spraying machine 800.

図11(a)で示す噴霧盤700は、椀内壁704と椀外壁706とが先端部708に向けて先細りの肉薄構造となるように構成されている。噴霧口702から噴霧された原料液は噴霧盤700の回転に伴い椀内壁704に沿って噴霧されることになる。これに対して、図11(b)で示す噴霧盤800においては、椀内壁804と椀外壁806とが先端部808に向けて涙滴形状が形成されるように、すなわち、椀外壁806と先端部808とを結ぶ線が円弧状(翼状)となるように椀壁自体の形状が転向部材として構成されることにより、椀外壁806に沿って流れる熱風等の高温ガスは、図中11(a)の矢印で示す直線的な流れとは異なり、図11(b)で示されるように椀内壁804側に流れ込むことになる。椀内壁804側に流れ込む高温ガスによって、噴霧口802から噴霧され、椀内壁804に沿って流れる原料液の噴流方向を鉛直下向き側方向に転向させることができる。これにより、噴霧された原料液は、十分な乾燥時間、距離が確保されるため、当該原料液を当該内側側壁に付着させることなく、適切に噴霧乾燥室500下部方向に導入することができる。 The spraying machine 700 shown in FIG. 11A is configured such that the bowl inner wall 704 and the bowl outer wall 706 have a thin wall structure that tapers toward the tip portion 708. The raw material liquid sprayed from the spray port 702 will be sprayed along the inner wall 704 of the bowl as the spraying machine 700 rotates. On the other hand, in the spray plate 800 shown in FIG. 11B, the bowl inner wall 804 and the bowl outer wall 806 form a teardrop shape toward the tip portion 808, that is, the bowl outer wall 806 and the tip end. Since the shape of the bowl wall itself is configured as a turning member so that the line connecting the portions 808 is arcuate (wing-shaped), the high-temperature gas such as hot air flowing along the bowl outer wall 806 is 11 (a) in the figure. ), The flow is different from the linear flow shown by the arrow of), and flows toward the inner wall 804 side of the bowl as shown in FIG. 11 (b). By the high temperature gas flowing into the bowl inner wall 804 side, the jet direction of the raw material liquid sprayed from the spray port 802 and flowing along the bowl inner wall 804 can be turned vertically downward. As a result, the sprayed raw material liquid can be appropriately introduced toward the lower part of the spray drying chamber 500 without adhering the raw material liquid to the inner side wall because a sufficient drying time and a sufficient distance are secured.

以上のように、本発明によれば、噴霧した原料液を乾燥部内側側壁に付着させることなく、乾燥部下部方向に適切に導入することが可能な噴霧盤、当該噴霧盤を用いた噴霧装置、及び当該噴霧装置を用いた噴霧乾燥装置を提供することができる。 As described above, according to the present invention, a spraying machine capable of appropriately introducing the sprayed raw material liquid toward the lower part of the drying part without adhering to the inner side wall of the drying part, and a spraying device using the spraying machine. , And a spray drying device using the spraying device can be provided.

なお、本発明に係る噴霧乾燥装置として、所謂、噴霧した原料液の液滴に含まれる溶媒を高温ガスとの接触により蒸発させ、乾燥するスプレードライヤ方式を採用する装置について説明したが、本発明はこれに限定されるものではなく、例えば、噴霧した原料液の液滴を低温環境下で凝結固化させ、これを凍結乾燥して乾燥粉体を得る噴霧凍結乾燥粉体製造装置に本発明を適用することも可能である。 As the spray drying device according to the present invention, a device adopting a so-called spray dryer method in which the solvent contained in the droplets of the sprayed raw material liquid is evaporated by contact with a high temperature gas and dried is described. Is not limited to this. It is also possible to apply.

10,60,70,90,600,620,640,700,800…噴霧盤、20…噴霧装置、30…原料液供給部、40…高温ガス供給部、50…噴霧乾燥装置、100,117,626、646…上側回転板、102…円環部、104…開口部、115…衝突ガイド部、101,106,109,628、648…下側回転板、108…平面部、110…回転軸接続部、112…ナット部、103a…第1傾斜片、103b…第2傾斜片、113,114、610、632,652…外縁部、103,107,111,116、612、634,654…エッジ部、118…ピン、120…皿ネジ、200…原料液供給管、202…モータ、204…カップリング、206・・・回転軸、208…上側軸支部、210…下側軸支部、212…ケーシング、214…取手、216…袋ナット、300…原料液タンク、302…ポンプ、304…原料液供給配管、400…ガス発生装置、402…ガス供給配管、404…ガス供給口、500…噴霧乾燥室、502…第1乾燥粉体回収部、504…衝撃・振動付与手段、506…天面、508…排気管、510…集塵装置、512…第2乾燥粉体回収部、514…エアーブルーム、602…ケスナー型噴霧機構、604、704、804…椀内壁、606…接続部、608…回転板、622…ベーン型噴霧機構、624,644,702,802…噴霧口、630,650…噴霧壁、642…スリットベーン型噴霧機構、700,900…噴霧盤、706,806…椀外壁、708,808…先端部 10,60,70,90,600,620,640,700,800 ... Sprayer, 20 ... Sprayer, 30 ... Raw material liquid supply unit, 40 ... High temperature gas supply unit, 50 ... Spray dryer, 100,117, 626, 646 ... upper rotating plate, 102 ... annular portion, 104 ... opening, 115 ... collision guide portion, 101, 106, 109, 628, 648 ... lower rotating plate, 108 ... flat portion, 110 ... rotating shaft connection Part, 112 ... Nut part, 103a ... First inclined piece, 103b ... Second inclined piece, 113, 114, 610, 632, 652 ... Outer edge part, 103, 107, 111, 116, 612, 634, 654 ... Edge part , 118 ... Pin, 120 ... Countersunk screw, 200 ... Raw material liquid supply pipe, 202 ... Motor, 204 ... Coupling, 206 ... Rotating shaft, 208 ... Upper shaft branch, 210 ... Lower shaft branch, 212 ... Casing, 214 ... handle, 216 ... cap nut, 300 ... raw material liquid tank, 302 ... pump, 304 ... raw material liquid supply pipe, 400 ... gas generator, 402 ... gas supply pipe, 404 ... gas supply port, 500 ... spray drying chamber, 502 ... 1st dry powder recovery unit, 504 ... Impact / vibration applying means, 506 ... Top surface, 508 ... Exhaust pipe, 510 ... Dust collector, 512 ... Second dry powder recovery unit, 514 ... Air bloom, 602 ... Kessner type spray mechanism, 604, 704, 804 ... Bowl inner wall, 606 ... Connection part, 608 ... Rotating plate, 622 ... Vane type spray mechanism, 624,644,702,802 ... Spray port, 630,650 ... Spray wall, 642 ... Slit vane type spray mechanism, 700, 900 ... Spray board, 706, 806 ... Bowl outer wall, 708, 808 ... Tip

Claims (9)

供給された原料液を所定の噴霧方向に噴霧する噴霧部材と、
前記原料液の前記噴霧方向を鉛直下向き側に転向させる転向部材とを備え、
前記噴霧部材は、中央部に開口部を有する上側回転板と、前記上側回転板と接続され、前記上側回転板に対して平行な平面を有する下側回転板とを含み
前記転向部材は、前記下側回転板の前記平面から鉛直下向き側に延在するエッジ部を有すること
を特徴とする噴霧盤。
A spraying member that sprays the supplied raw material liquid in a predetermined spraying direction,
A turning member for turning the spraying direction of the raw material liquid vertically downward is provided.
The spray member includes an upper rotary plate having an opening in the center and a lower rotary plate connected to the upper rotary plate and having a plane parallel to the upper rotary plate .
The turning member is a spraying machine characterized by having an edge portion extending vertically downward from the plane of the lower rotating plate.
前記下側回転板は円板状に形成され、前記エッジ部は前記平面の外縁部から円環状に延在する傾斜面として形成されること
を特徴とする請求項に記載の噴霧盤。
The spray disk according to claim 1 , wherein the lower rotary plate is formed in a disk shape, and the edge portion is formed as an inclined surface extending in an annular shape from the outer edge portion of the plane.
前記傾斜面は前記平面に対して5°~90°の傾斜を有すること
を特徴とする請求項に記載の噴霧盤。
The spraying machine according to claim 2 , wherein the inclined surface has an inclination of 5 ° to 90 ° with respect to the plane.
供給された原料液を所定の噴霧方向に噴霧する噴霧部材と、前記原料液の前記噴霧方向を鉛直下向き側に転向させる転向部材とを有する噴霧盤と、
前記噴霧盤に接続され、前記噴霧盤を所定の回転数で回転させる回転部とを備え、
前記噴霧部材は、中央部に開口部を有する上側回転板と、前記上側回転板と接続され、前記上側回転板に対して平行な平面を有する下側回転板とを含み、
前記転向部材は、前記下側回転板の前記平面から鉛直下向き側に延在するエッジ部を有すること
を特徴とする噴霧装置。
A spraying machine having a spraying member for spraying the supplied raw material liquid in a predetermined spraying direction, and a turning member for turning the spraying direction of the raw material liquid vertically downward.
It is provided with a rotating portion connected to the spraying machine and rotating the spraying machine at a predetermined rotation speed.
The spray member includes an upper rotary plate having an opening in the center and a lower rotary plate connected to the upper rotary plate and having a plane parallel to the upper rotary plate.
The turning member is a spraying device having an edge portion extending vertically downward from the plane of the lower rotating plate.
前記下側回転板は円板状に形成され、前記エッジ部は前記平面の外縁部から円環状に延在する傾斜面として形成されること
を特徴とする請求項に記載の噴霧装置。
The spraying device according to claim 4 , wherein the lower rotating plate is formed in a disk shape, and the edge portion is formed as an inclined surface extending in an annular shape from the outer edge portion of the plane.
前記傾斜面は前記平面に対して5°~90°の傾斜を有すること
を特徴とする請求項に記載の噴霧装置。
The spraying device according to claim 5 , wherein the inclined surface has an inclination of 5 ° to 90 ° with respect to the plane.
供給された原料液を所定の噴霧方向に噴霧する噴霧部材と、前記原料液の前記噴霧方向を鉛直下向き側に転向させる転向部材とを有する噴霧盤と、
前記噴霧盤に接続され、前記噴霧盤を所定の回転数で回転させる回転部と、
前記上側回転板の前記開口部を介して前記噴霧盤内部に原料液を供給する原料液供給部と、
前記噴霧盤から噴霧された前記原料液を乾燥することによって乾燥粉体を生成する粉体生成部とを備え、
前記噴霧部材は、中央部に開口部を有する上側回転板と、前記上側回転板と接続され、前記上側回転板に対して平行な平面を有する下側回転板とを含み、
前記転向部材は、前記下側回転板の前記平面から鉛直下向き側に延在するエッジ部を有すること
を特徴とする噴霧乾燥装置。
A spraying machine having a spraying member for spraying the supplied raw material liquid in a predetermined spraying direction, and a turning member for turning the spraying direction of the raw material liquid vertically downward.
A rotating part connected to the spraying machine and rotating the spraying machine at a predetermined rotation speed,
A raw material liquid supply unit that supplies the raw material liquid to the inside of the spray plate through the opening of the upper rotary plate, and a raw material liquid supply unit.
It is provided with a powder generating unit that produces dry powder by drying the raw material liquid sprayed from the spraying machine.
The spray member includes an upper rotary plate having an opening in the center and a lower rotary plate connected to the upper rotary plate and having a plane parallel to the upper rotary plate.
The spray drying device is characterized in that the turning member has an edge portion extending vertically downward from the plane of the lower rotating plate.
前記下側回転板は円板状に形成され、前記エッジ部は前記平面の外縁部から円環状に延在する傾斜面として形成されること
を特徴とする請求項に記載の噴霧乾燥装置。
The spray drying apparatus according to claim 7 , wherein the lower rotary plate is formed in a disk shape, and the edge portion is formed as an inclined surface extending in an annular shape from the outer edge portion of the plane.
前記傾斜面は前記平面に対して5°~90°の傾斜を有すること
を特徴とする請求項に記載の噴霧乾燥装置。
The spray drying device according to claim 8 , wherein the inclined surface has an inclination of 5 ° to 90 ° with respect to the plane.
JP2020520951A 2018-05-24 2018-05-24 Sprayer, sprayer, and spray dryer Active JP7007759B2 (en)

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006326393A (en) 2005-05-23 2006-12-07 Tdk Corp Spray disc, spray apparatus and spray dryer
JP2008207096A (en) 2007-02-26 2008-09-11 Jung-Won Kim Rotary automizer and air bearing protection system of the rotary automizer

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0641604Y2 (en) * 1989-11-24 1994-11-02 株式会社坂本技研 Spraying machine for spray dryer
JP2574918Y2 (en) * 1992-09-30 1998-06-18 京セラ株式会社 Sprayer of centrifugal sprayer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006326393A (en) 2005-05-23 2006-12-07 Tdk Corp Spray disc, spray apparatus and spray dryer
JP2008207096A (en) 2007-02-26 2008-09-11 Jung-Won Kim Rotary automizer and air bearing protection system of the rotary automizer

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