JPH02149333A - Apparatus for manufacturing spherical granules of oil material using organic solution as refrigerant - Google Patents

Apparatus for manufacturing spherical granules of oil material using organic solution as refrigerant

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Publication number
JPH02149333A
JPH02149333A JP63303007A JP30300788A JPH02149333A JP H02149333 A JPH02149333 A JP H02149333A JP 63303007 A JP63303007 A JP 63303007A JP 30300788 A JP30300788 A JP 30300788A JP H02149333 A JPH02149333 A JP H02149333A
Authority
JP
Japan
Prior art keywords
cooling liquid
granules
oil material
particles
liquid
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.)
Granted
Application number
JP63303007A
Other languages
Japanese (ja)
Other versions
JP2591671B2 (en
Inventor
Atsumi Tobiya
飛谷 篤実
Toshimitsu Yoshioka
吉岡 俊満
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Snow Brand Milk Products Co Ltd
Original Assignee
Snow Brand Milk Products Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Snow Brand Milk Products Co Ltd filed Critical Snow Brand Milk Products Co Ltd
Priority to JP30300788A priority Critical patent/JP2591671B2/en
Publication of JPH02149333A publication Critical patent/JPH02149333A/en
Application granted granted Critical
Publication of JP2591671B2 publication Critical patent/JP2591671B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To prevent dropping granules from coagulating by forming a swirl in a horizontal direction in the surface of the cooling liquid by stirring fan at the time of cooling and solidifying granules of a molten oil material in the inside of concentric double cylinders. CONSTITUTION:Granules of a molten oil material are dropped to a cooling liquid in the inside of an inner cylinder 2 of inner and outer double cylinders 1, 2 and solidified while descending to form granular powder. A stirring fan 18 rotatable in a rotating frequency enough to produce a swirl of the cooling liquid in the horizontal direction is installed near surface area of the cooling liquid in the inside of the cylinder 2 to which the molten oil material is dropped. As a result, dropping granules are prevented from colliding an coagulating with other granules and spherical granules of the oil material are continuously and efficiently manufactured.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、医薬品、食品、飼料さらには触媒、カーボン
等の工業月料の製造加工に適した油性物質の球形粉粒体
の製造装置に関するものである。
Detailed Description of the Invention (Field of Industrial Application) The present invention relates to an apparatus for producing spherical powder of an oily substance suitable for manufacturing and processing pharmaceuticals, foods, feeds, and industrial materials such as catalysts and carbon. It is something.

(従来の技術) 球形粉粒体を製造する装置としては、特公昭51−88
75号公報や特公昭60−2904号公報に示されたも
のがある。
(Prior art) As an apparatus for manufacturing spherical powder, the Japanese Patent Publication No. 51-88
Some of these are disclosed in Japanese Patent Publication No. 75 and Japanese Patent Publication No. 60-2904.

前者のものは、同心二重円筒からなる冷却部と逆U字管
を有する回収部とで構成され、冷却部上部の内円筒内に
下向きに取付けた二重ノズルから、液状のカプセル化物
質とカプセル充填物とを複合ジェット流として内円筒内
の冷却液中に押出し、冷却液と共に内円筒中を降下する
間に造粒作用を行わせて粉粒体を形成するもので生成さ
れた粒子は、冷却器下部から回収部へ送られ、篩によっ
て液から粉粒体が分離回収されるようになっている。
The former consists of a cooling section consisting of a concentric double cylinder and a recovery section having an inverted U-shaped tube, and the liquid encapsulated material is collected from a double nozzle installed downward in the inner cylinder at the top of the cooling section. The particles produced by extruding the capsule filling material into the cooling liquid in the inner cylinder as a composite jet stream, and performing a granulation action while descending in the inner cylinder together with the cooling liquid to form powder and granules. The liquid is sent from the lower part of the cooler to the recovery section, and the powder and granules are separated and recovered from the liquid using a sieve.

後者のものは、カプセルの反応槽と回収槽で構成され、
回収槽にスクリューコンヘアが有孔円筒内に取付けられ
た分離器を用いることを特徴としている。
The latter one consists of a capsule reaction tank and collection tank;
It is characterized by using a separator in which a screw conhair is installed in a perforated cylinder in the recovery tank.

(発明が解決しようとする課題) 前述した従来の前者のものは、ゼラチン等のような緩や
かに固化する物質には有効であるが、油性物質の粒子を
製造する際には、ノズルの先端を冷却液中に入れること
によって油性物質が固化してノズルが閉塞するという問
題がおきる。
(Problem to be Solved by the Invention) The former method described above is effective for materials that harden slowly, such as gelatin, but when producing particles of oily substances, the tip of the nozzle must be A problem arises in that the oily substance solidifies and blocks the nozzle when placed in the coolant.

又、ノズルを液面より上方に取付けた場合には、先に落
下した粒子が後からくる粒子と衝突して凝集するという
欠点がある。
In addition, when the nozzle is installed above the liquid level, there is a drawback that the particles that fall first collide with the particles that come later and agglomerate.

後者のものは、ノズル近傍の冷却液の整流が不十分なた
め、滴下した粒子が液面付近で他の粒子と衝突して凝集
するという欠点がある。
The latter method has the disadvantage that, because the cooling liquid near the nozzle is not sufficiently rectified, the dropped particles collide with other particles near the liquid surface and agglomerate.

したがって、油性物質の粒子を製造する場合に、この装
置を利用することによって所望の粒径及び形状の粒子を
得ることは非常に難しい。
Therefore, when producing particles of an oily substance, it is very difficult to obtain particles with a desired particle size and shape by using this apparatus.

したがって、本案は、滴下した粒子が他の粒子と衝突し
て凝集するということのない、有機溶液を冷媒に用いて
油性物質の球形粉粒体を製造する装置を得ることを目的
とするものである。
Therefore, the purpose of the present invention is to obtain an apparatus for producing spherical powder of an oily substance using an organic solution as a refrigerant, in which dropped particles do not collide with other particles and agglomerate. be.

(課題を解決するための手段) 本案は以上のような目的を達成するため、次に述べる構
成を有する装置を提供するものである。
(Means for Solving the Problems) In order to achieve the above objects, the present invention provides an apparatus having the following configuration.

すなわち、溶融した油性物質の粒子を内外−重円筒から
なるその内円筒内の冷却液中に滴下して降下させながら
、固化させて粉粒体を形成させる装置において、溶融し
た油性物質を滴下する内円筒の冷却液面付近に冷却液を
水平方向に旋回流を生じせしめる回転数可変の攪拌羽根
を設置したことを特徴とする有機溶液を冷媒に用いて油
性物質の球形粉粒体を製造する装置である。
That is, the molten oily substance is dropped into a cooling liquid in an inner cylinder consisting of an inner and outer heavy cylinder, and the molten oily substance is dropped in a device that solidifies and forms powder while falling. A spherical powder of an oily substance is produced using an organic solution as a refrigerant, characterized in that stirring blades with a variable rotation speed are installed near the cooling liquid surface in an inner cylinder to generate a horizontal swirling flow of the cooling liquid. It is a device.

(作用) 加温溶媒した油性物質からなる粒子は、同心二重円筒の
円筒内において有機溶液によって冷却固化されるが、攪
拌羽根によって冷却液面には水平方向の旋回流が生じて
いるので滴下する粒子は凝集することはない。
(Function) Particles made of an oily substance heated in a solvent are cooled and solidified by an organic solution in a concentric double cylinder, but since a horizontal swirling flow is generated on the surface of the cooling liquid by the stirring blade, the particles drop. particles that do not clump together.

(実施例) 以下、図面に示す実施例について説明する。(Example) The embodiments shown in the drawings will be described below.

本発明においては、球形粉粒体を効率よく製造するため
に、有機溶液を冷媒として用いるもので、熔融した油性
物質としては油脂類、ワックス類及び樹脂類からなる群
から選択されたものの1種もしくは混合物を用いる。
In the present invention, in order to efficiently produce spherical powder, an organic solution is used as a refrigerant, and the molten oily substance is one selected from the group consisting of oils and fats, waxes, and resins. Or use a mixture.

又、溶融した油性物質の粒子は、単一粒子、芯部を有す
るカプセル及びエマルションや分散液からなる粒子のい
ずれかの形態からなるものを用いるものであり、有機溶
液を冷媒として用いる場合、油性物質の比重より小さい
かほぼ等しい比重を有し、かつ油性物質に対して十分に
大きな界面張力を示す単一成分、もしくは多成分系の有
機液体又はその水溶液であるものを用いる。
In addition, the particles of the molten oil-based substance are in the form of a single particle, a capsule with a core, or a particle consisting of an emulsion or dispersion. When an organic solution is used as a refrigerant, A single-component or multi-component organic liquid or an aqueous solution thereof having a specific gravity smaller than or almost equal to the specific gravity of the substance and exhibiting a sufficiently large interfacial tension with respect to the oily substance is used.

次に、以上のような油性物質と、有機溶液を用いて球形
粉粒体を製造する装置について説明すると、粒径が10
0μm〜5mnのものの製造は第1図に示すようなもの
で、冷却部と回収部とからなり、冷却部は同心二重円筒
(1)(2)からなり、内円筒(2)の下端はホーン状
に開口させてその外周縁を外筒(1)に取り付けて硬化
槽(3)を形成している。硬化槽(3)からU字形の回
収管(4)を介して回収部が形成されている。回収部に
は回収管(4)につながる外円筒(5)があり、外円筒
(5)の上部は回収槽(6)を貫通して回収塔を形成し
ている。
Next, we will explain the apparatus for producing spherical powder using the above-mentioned oil-based substance and organic solution.
The manufacturing process for 0 μm to 5 mm is as shown in Figure 1, which consists of a cooling section and a recovery section. The cooling section consists of concentric double cylinders (1) and (2), and the lower end of the inner cylinder (2) is A curing tank (3) is formed by opening in a horn shape and attaching its outer peripheral edge to an outer cylinder (1). A recovery section is formed from the curing tank (3) via a U-shaped recovery pipe (4). The recovery section has an outer cylinder (5) connected to a recovery pipe (4), and the upper part of the outer cylinder (5) passes through a recovery tank (6) to form a recovery tower.

外円筒(5)内には、スクリューコンベア(7)が取り
付けられており、外円筒(5)の開口部には無数の孔(
8)が形成された粒子取出し樋(9)が下向き傾斜に設
けられ、取出し樋(9)の下端は製品タンク(10)に
臨んでいる。
A screw conveyor (7) is installed inside the outer cylinder (5), and numerous holes (
A particle take-out gutter (9) having a particle take-out gutter (9) formed therein is tilted downward, and the lower end of the take-out gutter (9) faces the product tank (10).

図示のものではスクリューコンベア(7)のスクリュ一
端部が取出し樋(9)より上方に突出し、モーター(1
1)で駆動されるようになっている。
In the illustrated example, one end of the screw of the screw conveyor (7) protrudes above the take-out gutter (9), and the motor (1)
1).

回収槽(6)は回収液管(12)につながっており、こ
の回収液管(12)は流量可変ポンプ(13)を介して
冷却液体の温度を一定に制御する熱交換器(14)につ
ながり、返送管(15)で冷却部の外円筒(1)に返送
されるようになっている。
The recovery tank (6) is connected to a recovery liquid pipe (12), and this recovery liquid pipe (12) is connected to a heat exchanger (14) that controls the temperature of the cooling liquid at a constant level via a variable flow rate pump (13). The water is connected to the outer cylinder (1) of the cooling section through a return pipe (15).

さて多重ノズル又は単一ノズル(16)から内円筒(2
)の冷却液中に油性物質、若しくはカプセル化物質とカ
プセル充填物質を滴下する。
Now, from the multiple nozzle or single nozzle (16) to the inner cylinder (2
) Drop the oily substance or the encapsulating substance and the capsule filling substance into the cooling liquid.

そして、内円筒中を降下しながら造粒され、造粒された
ものはU字管(4)を経て外円筒(5)のスクリューコ
ンベア(7)で上昇するが、その際粒子体はスクリュー
コンベア(7)で液中から運び上げられ、粒子取出し樋
(9)上に飛び出る。粒子取出し樋(9)に送られた液
はその孔(8)から回収槽(6)に回収され、回収液管
(12)を経て、熱交換器(14)で冷却されて返送管
(15)から外円筒(1)の冷却液中に返送される。以
上のような液の循環は流量可変ポンプ(13)によって
なされる。
Then, the granules are granulated while descending in the inner cylinder, and the granulated material passes through the U-shaped pipe (4) and ascends on the screw conveyor (7) in the outer cylinder (5). (7), the particles are lifted out of the liquid and pop out onto the particle extraction gutter (9). The liquid sent to the particle extraction gutter (9) is collected from the hole (8) into the recovery tank (6), passes through the recovery liquid pipe (12), is cooled by the heat exchanger (14), and is sent to the return pipe (15). ) into the cooling liquid of the outer cylinder (1). The liquid circulation as described above is performed by a variable flow rate pump (13).

本発明は以上のような油性物質、又はカプセル化物質と
カプセル充填物とを単一ノズル、又は多重ノズルで滴下
する内円筒の冷却液面イ]近に水平方向に冷却液の旋回
流を生じせしめる回転数可変の攪拌羽根(18)を設置
したものである。
The present invention produces a swirling flow of the cooling liquid in the horizontal direction near the cooling liquid surface of the inner cylinder where the oily substance or the encapsulating substance and the capsule filler are dropped using a single nozzle or multiple nozzles. It is equipped with a stirring blade (18) whose rotation speed is variable.

第2図に示すように外円筒(1)の所定の位置に設けた
返送管(15)の液流入口(17)より入った冷却液は
内外円筒間を上向きに流れ、内円筒(2)内に流れ込む
。内円筒(2)の上端には回転軸(19)に固定した攪
拌羽根(18)を臨ませ、モーター(20)を用いて回
転させることにより冷却液面近傍に水平方向の旋回流が
生じる。
As shown in Fig. 2, the cooling liquid enters from the liquid inlet (17) of the return pipe (15) provided at a predetermined position of the outer cylinder (1), flows upward between the inner and outer cylinders, and flows upwardly into the inner cylinder (2). Flow inside. A stirring blade (18) fixed to a rotating shaft (19) faces the upper end of the inner cylinder (2), and is rotated using a motor (20) to generate a horizontal swirling flow near the coolant surface.

冷却液面の上方より加温溶融した油性物質からなる油性
物質の粒子を滴下する。冷却液に落下した粒子は攪拌羽
根(18)により旋回流に乗って迅速に水平方向に移動
しながら沈降する。
Particles of an oily substance made of heated and melted oily substance are dropped from above the surface of the coolant. The particles that have fallen into the cooling liquid are quickly moved horizontally in a swirling flow by the stirring blade (18) and settle down.

粒子は冷却液中を沈降しながら冷却固化し、外円筒(1
)の底部からU字管(4)に向かって冷却液と共に流出
する。
The particles cool and solidify while settling in the cooling liquid, forming an outer cylinder (1
) flows out along with the cooling liquid toward the U-shaped tube (4).

前述した如く、回収槽(6)で粒子から分離回収された
冷却液はポンプ(13)により熱交換器へ送られ温度調
整されてからさらに冷却部の液流入口(17)へ戻され
る。
As described above, the coolant separated and recovered from the particles in the recovery tank (6) is sent to the heat exchanger by the pump (13), temperature-adjusted, and then returned to the liquid inlet (17) of the cooling section.

冷却部の液面の高さの調整はポンプ(13)の流量を変
えることにより行われる。
The height of the liquid level in the cooling section is adjusted by changing the flow rate of the pump (13).

なお、スクリューコンベア(7)の回転により流量調節
をすることができるが、オーバーフローによる液面調節
はあってもなくともよい。
Although the flow rate can be adjusted by rotating the screw conveyor (7), the liquid level may or may not be adjusted by overflow.

又ノズルは内円筒の液中にあると油性物質が固化してノ
ズルを閉塞してしまうため、ノズルは液面より上方に配
置される。
Furthermore, if the nozzle is submerged in the liquid in the inner cylinder, the oily substance will solidify and block the nozzle, so the nozzle is arranged above the liquid level.

第3図に示すものは、粒径が500μm以下の小さいも
のに使用されるものであって、硬化槽(3)の下端に分
離器を設けたもので構成される。
The one shown in FIG. 3 is used for small particles with a particle size of 500 μm or less, and is constructed by providing a separator at the lower end of a curing tank (3).

(19)は篩の形成された粒子取出し樋であって製品タ
ンク(10)につながっていることは第1図のものと同
様であるが、流量調節弁(20)が粒子取出し樋(19
)の上方にあり、又ポンプ(13)と熱交換器(14)
との間にも流量調節弁(21)がある。
(19) is a particle extraction gutter with a sieve formed thereon, and is connected to the product tank (10), which is the same as in Fig. 1, but the flow rate control valve (20) is connected to the particle extraction gutter (19).
) above the pump (13) and heat exchanger (14).
There is also a flow control valve (21) between the two.

もっともポンプ(13)が流量可変ポンプであれば流量
調節弁はいらない。
However, if the pump (13) is a variable flow rate pump, there is no need for a flow rate control valve.

(発明の効果) 本発明によれば油性物質が滴下される内円筒内の液面は
、撹拌羽根で水平方向の旋回流が生じているので滴下さ
れた粒子同士が凝集することはない。
(Effects of the Invention) According to the present invention, since a horizontal swirling flow is generated by the stirring blades on the liquid surface in the inner cylinder onto which the oily substance is dropped, the dropped particles do not aggregate with each other.

一般に冷却液の流れの状態は粒子の径や形状に大きく影
響するので冷却液の整流は重要であるが、本命明では攪
拌羽根の形状や回転数を変えることによって冷却液面近
傍の流れを調整することもできる。
In general, the flow condition of the coolant greatly affects the diameter and shape of the particles, so rectifying the coolant is important, but in Honmeimei, the flow near the coolant surface is adjusted by changing the shape and rotation speed of the stirring blade. You can also.

したがって、本発明によると粒子の凝集を防止するだけ
でなく冷却液の流れを制御し、所定の径、及び形状の粒
子を製造することが可能となる。
Therefore, according to the present invention, it is possible not only to prevent particle agglomeration but also to control the flow of the cooling liquid to produce particles with a predetermined diameter and shape.

何れにしても本発明装置によると油性物質の球形粉粒体
を連続的に効率よく製造することができる。
In any case, according to the apparatus of the present invention, spherical powder of oily substances can be produced continuously and efficiently.

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

第1図は第1実施例にかかる氷室装置の概略図、 第2図(イ)(ロ)は撹拌羽根のある部分の説明図、 第3図は第2実施例にかかる氷室装置の概略図である。 (1)・・・・・外円筒 (2)・・・・・内円筒 (6)・・・・・回収槽 (10)・・・・・製品タンク (12)・・・・・回収液管 (13)・・・・・ポンプ (14)・・・・・熱交換器 (16)・・・・・ノズル (18)・・・・・攪拌羽根 FIG. 1 is a schematic diagram of the ice chamber apparatus according to the first embodiment; Figure 2 (a) and (b) are explanatory diagrams of the part with stirring blades, FIG. 3 is a schematic diagram of the ice chamber apparatus according to the second embodiment. (1)・・・Outer cylinder (2) Inner cylinder (6)・・・Recovery tank (10)・・・Product tank (12)・・・Collection liquid pipe (13)・・・Pump (14)・・・Heat exchanger (16)・・・Nozzle (18)・・・Stirring blade

Claims (1)

【特許請求の範囲】[Claims] 溶融した油性物質の粒子を、内外二重円筒からなるその
内円筒内の冷却液中に滴下して降下させながら固化させ
て粉粒体を形成させる装置において、溶融した油性物質
を滴下する内円筒の冷却液面付近に、水平方向に冷却液
の旋回流を生じせしめる回転数可変の攪拌羽根を設置し
たことを特徴とする有機溶液を冷媒に用いて油性物質の
球形粉粒体を製造する装置。
An inner cylinder into which the molten oily substance is dripped, in a device in which particles of the molten oily substance are dropped into a cooling liquid in an inner cylinder consisting of an inner and outer double cylinder, and solidified as they fall to form powder. An apparatus for producing spherical powder of an oil-based substance using an organic solution as a refrigerant, characterized in that a stirring blade with a variable rotation speed is installed near the surface of the cooling liquid to generate a swirling flow of the cooling liquid in the horizontal direction. .
JP30300788A 1988-11-30 1988-11-30 Apparatus for producing spherical particles of oily substance using organic solution as refrigerant Expired - Lifetime JP2591671B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30300788A JP2591671B2 (en) 1988-11-30 1988-11-30 Apparatus for producing spherical particles of oily substance using organic solution as refrigerant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30300788A JP2591671B2 (en) 1988-11-30 1988-11-30 Apparatus for producing spherical particles of oily substance using organic solution as refrigerant

Publications (2)

Publication Number Publication Date
JPH02149333A true JPH02149333A (en) 1990-06-07
JP2591671B2 JP2591671B2 (en) 1997-03-19

Family

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Country Status (1)

Country Link
JP (1) JP2591671B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002095951A (en) * 2000-09-26 2002-04-02 Isao Yokoyama Manufacturing method for particulate gel and manufacturing device
JP2008190788A (en) * 2007-02-05 2008-08-21 Takasago Thermal Eng Co Ltd Maintenance device of heat exchanger

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CN109692126B (en) * 2019-03-01 2021-10-22 深圳万和制药有限公司 Method for preparing high-uniformity dropping pills and equipment used by same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002095951A (en) * 2000-09-26 2002-04-02 Isao Yokoyama Manufacturing method for particulate gel and manufacturing device
JP4546631B2 (en) * 2000-09-26 2010-09-15 功 横山 Method and apparatus for producing granular gel body
JP2008190788A (en) * 2007-02-05 2008-08-21 Takasago Thermal Eng Co Ltd Maintenance device of heat exchanger

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