JP3000323B2 - Centrifugal spray device - Google Patents
Centrifugal spray deviceInfo
- Publication number
- JP3000323B2 JP3000323B2 JP4315366A JP31536692A JP3000323B2 JP 3000323 B2 JP3000323 B2 JP 3000323B2 JP 4315366 A JP4315366 A JP 4315366A JP 31536692 A JP31536692 A JP 31536692A JP 3000323 B2 JP3000323 B2 JP 3000323B2
- Authority
- JP
- Japan
- Prior art keywords
- rotating disk
- particle size
- disk
- fluid
- powder
- 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.)
- Expired - Lifetime
Links
- 239000007921 spray Substances 0.000 title description 6
- 239000012530 fluid Substances 0.000 claims description 17
- 238000005507 spraying Methods 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 18
- 239000002245 particle Substances 0.000 description 16
- 239000000843 powder Substances 0.000 description 14
- 229910052757 nitrogen Inorganic materials 0.000 description 9
- 239000010419 fine particle Substances 0.000 description 6
- 239000004677 Nylon Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 230000005674 electromagnetic induction Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 229920001778 nylon Polymers 0.000 description 3
- 239000007789 gas Substances 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 description 1
- 229920000299 Nylon 12 Polymers 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/10—Making granules by moulding the material, i.e. treating it in the molten state
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
- B29B2009/125—Micropellets, microgranules, microparticles
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Glanulating (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は回転円盤による流体の遠
心噴霧装置に関し、更に詳細には粒度分布のシャープな
微粒子を得るための遠心噴霧装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a centrifugal spraying device for a fluid using a rotating disk, and more particularly to a centrifugal spraying device for obtaining fine particles having a sharp particle size distribution.
【0002】[0002]
【従来技術および発明が解決しようとする課題】回転円
盤上に溶液、融液、スラリー、エマルジョン等の流体を
供給し、遠心力でこれを噴霧し液滴を形成し、これを乾
燥または冷却固化して、主に球状の粉体を得ることは広
く行われている。この造粒方法は特に回転円盤の回転速
度を変える等の方法で、比較的容易に平均粒度を変えら
れる利点がある。しかしながら粒度分布をシャープにす
ることと、微粒子粉体を得ることについては未だ課題を
残している。2. Description of the Related Art Fluids such as solutions, melts, slurries and emulsions are supplied onto a rotating disk and sprayed by centrifugal force to form droplets, which are dried or cooled and solidified. It is widely practiced to obtain mainly spherical powder. This granulation method has an advantage that the average particle size can be relatively easily changed by changing the rotation speed of the rotating disk. However, there is still a problem in sharpening the particle size distribution and obtaining fine particle powder.
【0003】粒度分布をシャープにすることは、事業上
重要なことである。なぜなら一般にこのような粉体の用
途においては、粒度分布を指定されることが多く、得ら
れた粉体の粒度分布が広いと分級せざるを得ず、分級に
よって目的の粒度から外れた部分が使用できず無駄とな
る。また、一般に粉体は微粒子のもの程市場価格が高く
なる傾向にある。[0003] Sharpening the particle size distribution is important in business. In general, in the use of such powders, the particle size distribution is often specified, and if the particle size distribution of the obtained powder is wide, classification must be performed. It cannot be used and is wasted. In general, the finer the powder, the higher the market price tends to be.
【0004】回転円盤による遠心噴霧で粒度分布のシャ
ープな微粉を得るためには、供給される流体を円盤上全
面に、均一な厚みのフィルム状に広げることが有効であ
る。しかし、回転円盤上に供給された液体は、供給され
た位置からそのまま円盤上を周辺に向って流れ、従って
円盤上の一部のみが噴霧に利用されるだけであり、流れ
る流体の厚さも均一にはならない。これを防ぐために回
転円盤上に数個所から液体を供給したり、円盤の軸の周
囲にドーナツ状流体供給管を設けたりすることが行われ
ているが、満足すべきシャープな粒度分布を持った微粒
子粉体が得られていないのが現状である。[0004] In order to obtain fine powder having a sharp particle size distribution by centrifugal spraying with a rotating disk, it is effective to spread the supplied fluid over the entire surface of the disk into a film having a uniform thickness. However, the liquid supplied on the rotating disk flows from the supplied position to the periphery of the disk as it is, so only a part of the disk is used for spraying, and the thickness of the flowing fluid is uniform. It does not become. In order to prevent this, liquid is supplied from several places on the rotating disk, and donut-shaped fluid supply pipes are provided around the axis of the disk, but it has a satisfactory sharp particle size distribution At present, fine particle powder has not been obtained.
【0005】本発明の目的は、回転円盤上全体に流体を
均一に広げて噴霧し、均一な微液滴を作ることにより、
粒度分布のシャープな微粒子粉体を得ることにある。本
発明者は、流体を均一に広げるためには、遠心力がゼロ
である回転円盤の中心に液を供給すべきことに着目し、
しかも得られた粉体の回収の容易さから、円盤の回転駆
動装置は回転円盤の上方に設けるべきであることを考慮
して本発明に達したものである。[0005] An object of the present invention is to uniformly spread a fluid on a rotating disk and spray it to form uniform fine droplets.
An object is to obtain fine particle powder having a sharp particle size distribution. The present inventors have noticed that in order to spread the fluid uniformly, the liquid should be supplied to the center of the rotating disk where the centrifugal force is zero,
In addition, the present invention has been made in consideration of the fact that the rotation driving device for the disk should be provided above the rotary disk in order to facilitate the collection of the obtained powder.
【0006】[0006]
【課題を解決するための手段】すなわち本発明は、上部
よりの駆動軸によって回転する下面が下方に凹である回
転円盤の下面の中心部に、下方より流体を供給すること
を特徴とする回転円盤による遠心噴霧装置を提供するも
のである。That is, according to the present invention, a fluid is supplied from below to a center portion of a lower surface of a rotating disk whose lower surface is rotated downward by a drive shaft from above. A centrifugal spray device using a disk is provided.
【0007】本発明に用いられるディスクは、遠心力に
よって流体が回転円盤下面上を流れるため、回転円盤の
下面は下方に凹である必要がある。回転円盤の周辺に
は、たとえばスプロケット状とする等各種の細工を加え
ることができる。In the disk used in the present invention, since the fluid flows on the lower surface of the rotating disk due to centrifugal force, the lower surface of the rotating disk needs to be concave downward. Various modifications such as a sprocket shape can be added around the rotating disk.
【0008】また回転円盤の上方及び/又は下方より加
熱あるいは冷却気体を吹き付けることができる。特に下
方より気体を吹き付ける場合は、気体供給管の中に流体
供給管を通すことができる。Further, a heating or cooling gas can be blown from above and / or below the rotating disk. Particularly when the gas is blown from below, the fluid supply pipe can be passed through the gas supply pipe.
【0009】更に、回転円盤を円盤上部より電磁誘導加
熱すれば、最も有利に冷却造粒により粒度分布のシャー
プな微粒子粉体が得られる。Further, if the rotating disk is heated by electromagnetic induction from above the disk, it is most advantageous to obtain a fine particle powder having a sharp particle size distribution by cooling granulation.
【0010】[0010]
【発明の効果】本発明によれば、回転円盤上全体に流体
が均一に広がるため、粒度分布のシャープな微粒子粉体
を作ることができる。According to the present invention, since the fluid uniformly spreads over the entire rotating disk, fine particle powder having a sharp particle size distribution can be produced.
【0011】[0011]
【実施例】大川原化工機(株)製スプレードライヤーO
C−16を用いて実施した。図1に示すようにディスク
1の上、下方向より250℃の熱窒素を吹きつけ、下方
の窒素吹込管中を通っている流体供給管より回転円盤
(110mmφ)の中心に5kg/時で、250℃の溶
融ナイロンにオリゴマー(数平均分子量4000)を供
給した。回転円盤は電磁誘導加熱によって300℃に加
熱し、2500rpmで回転させた。冷却用窒素の温度
は40℃、窒素排出管での窒素温度は100℃あった。
得られたナイロンにオリゴマー粉体は球状で、レーザー
粒度分布測定機(島津製作所(株)製SALD110
0)によれば平均粒度20μm、5μm〜25μmの粒
度の部分が83重量%であった。[Example] Okawara Kakoki Co., Ltd. spray dryer O
Performed using C-16. As shown in FIG. 1, hot nitrogen of 250 ° C. is blown from above and below the disk 1, and 5 kg / hour is applied to the center of a rotating disk (110 mmφ) from a fluid supply pipe passing through a nitrogen blow pipe below. Oligomers (number average molecular weight 4000) were supplied to molten nylon at 250 ° C. The rotating disk was heated to 300 ° C. by electromagnetic induction heating and rotated at 2500 rpm. The temperature of the cooling nitrogen was 40 ° C., and the nitrogen temperature at the nitrogen exhaust tube was 100 ° C.
In the obtained nylon, the oligomer powder is spherical, and a laser particle size distribution analyzer (SALD110 manufactured by Shimadzu Corporation)
According to 0), the portion having an average particle size of 20 μm and a particle size of 5 μm to 25 μm was 83% by weight.
【0012】[0012]
【比較例】回転円盤として、白熱電球の笠状であり、上
方より供給された流体が回転円盤分の穴を通り円盤下面
に流れるようになっている直径110mmφの円盤を用
いた。図2のように回転円盤を取り付け、上方よりナイ
ロン12オリゴマーを供給する以外実施例と同一の条件
でナイロンにオリゴマー粉体を得た。粉体は球状で実施
例1と同様の測定によれば、平均粒度72μm、60μ
m〜80μmの粒度の部分は32重量%であった。COMPARATIVE EXAMPLE As a rotating disk, a disk having a diameter of 110 mm was used, which was in the shape of a cap of an incandescent light bulb, and through which the fluid supplied from above passed through the hole of the rotating disk and flowed to the lower surface of the disk. As shown in FIG. 2, an oligomer powder was obtained on nylon under the same conditions as in the example except that a rotating disk was attached and nylon 12 oligomer was supplied from above. According to the same measurement as in Example 1, the powder was spherical and had an average particle size of 72 μm and 60 μm.
The fraction with a particle size of m to 80 μm was 32% by weight.
【図1】本発明の回転円盤による遠心噴霧装置の図。FIG. 1 is a diagram of a centrifugal spray device using a rotating disk according to the present invention.
【図2】上方より流体を供給する遠心噴霧装置の要部
図。FIG. 2 is a main part view of a centrifugal spray device for supplying a fluid from above.
1 回転円盤 2 モーター 3 軸 4 電磁誘導加熱装置 5 上部熱窒素吹込管 6 下部熱窒素吹込管 7 流体供給管 8 冷却用窒素吹込管 9 窒素排出管 10 流体の流れる穴 Reference Signs List 1 rotating disk 2 motor 3 shaft 4 electromagnetic induction heating device 5 upper thermal nitrogen injection pipe 6 lower thermal nitrogen injection pipe 7 fluid supply pipe 8 cooling nitrogen injection pipe 9 nitrogen discharge pipe 10 hole through which fluid flows
Claims (1)
が下方に凹である回転円盤の下面の中心部に、下方より
流体を供給して遠心噴霧させることを特徴とする回転円
盤による遠心噴霧装置。1. A centrifugal spraying device using a rotating disk, wherein a fluid is supplied from below to a central portion of a lower surface of a rotating disk whose lower surface is rotated downward by a drive shaft from above and is centrifugally sprayed. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4315366A JP3000323B2 (en) | 1992-11-25 | 1992-11-25 | Centrifugal spray device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4315366A JP3000323B2 (en) | 1992-11-25 | 1992-11-25 | Centrifugal spray device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06155457A JPH06155457A (en) | 1994-06-03 |
| JP3000323B2 true JP3000323B2 (en) | 2000-01-17 |
Family
ID=18064551
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4315366A Expired - Lifetime JP3000323B2 (en) | 1992-11-25 | 1992-11-25 | Centrifugal spray device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3000323B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI785881B (en) * | 2019-06-28 | 2022-12-01 | 美商壹久公司 | System and process with assisted gas flow inside a reaction chamber |
| CN114602198B (en) * | 2022-03-24 | 2023-11-24 | 山东卫康生物医药科技有限公司 | Functional chitosan oligosaccharide preparation is with antiseized wall centrifugal spray drying device |
-
1992
- 1992-11-25 JP JP4315366A patent/JP3000323B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06155457A (en) | 1994-06-03 |
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