JPH07289876A - Granulating and drying method of powder material - Google Patents
Granulating and drying method of powder materialInfo
- Publication number
- JPH07289876A JPH07289876A JP6086231A JP8623194A JPH07289876A JP H07289876 A JPH07289876 A JP H07289876A JP 6086231 A JP6086231 A JP 6086231A JP 8623194 A JP8623194 A JP 8623194A JP H07289876 A JPH07289876 A JP H07289876A
- Authority
- JP
- Japan
- Prior art keywords
- granulated product
- granulated
- granulating
- screen
- product
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、粉体の湿式造粒乾燥方
法に関し、更に詳しくは、造粒品のブロッキングを防止
し、目的とする造粒乾燥物を高収率で得る方法に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wet granulation / drying method for powders, and more particularly to a method for preventing a granulated product from blocking and obtaining a desired granulated dried product in a high yield. Is.
【0002】[0002]
【従来技術及びその問題点】従来、湿式造粒品を乾燥す
る際、湿式造粒品を直接乾燥機に投入する方法が行われ
ている。しかし、この方法では造粒品が相互に付着して
ブロックを形成したり、乾燥機内壁に付着して目的とす
る造粒乾燥物を20〜40%程度しか得られず、種々条
件を工夫しても収率はせいぜい60%まで向上させるの
が限度であった。2. Description of the Related Art Conventionally, when a wet-granulated product is dried, a method of directly introducing the wet-granulated product into a dryer has been used. However, in this method, the granulated products adhere to each other to form blocks, or only 20 to 40% of the target granulated dried product adhered to the inner wall of the dryer can be obtained, and various conditions are devised. However, the maximum yield was limited to 60%.
【0003】[0003]
【発明の課題】粉体の湿式造粒品を乾燥する際、造粒品
のブロッキングを防止し、目的とする造粒乾燥物を高収
率で得ることを課題とする。An object of the present invention is to prevent the granulated product from blocking when drying the wet granulated product of the powder and to obtain the target granulated dried product in a high yield.
【0004】[0004]
【課題を解決するための手段】湿式造粒において乾燥機
に投入する際、従来法では造粒物同士が相互に付着して
3〜100mmの大きな塊を形成し(ブロッキング)目
的とする造粒物が30〜40%しか得られなかった。そ
こで発明者等は目的とする造粒物をいかに高収率で得る
か、種々検討した。Means for Solving the Problems In the wet granulation, when the granules are put into a dryer, the granules adhere to each other to form a large lump of 3 to 100 mm in the conventional method (blocking). Only 30-40% was obtained. Therefore, the inventors conducted various studies on how to obtain the target granulated product in high yield.
【0005】その結果、造粒機から造粒品を乾燥機に投
入する際、目的の造粒品より大きな開口のスクリーン等
を通して乾燥機に投入することにより、ブロッキングが
防止され目的物の収率が著しく向上できるとの知見に到
り、本発明を完成したものである。As a result, when the granulated product is put into the dryer from the granulator, blocking is prevented by introducing the granulated product into the dryer through a screen having an opening larger than that of the target granulated product. The present invention has been completed based on the finding that the above can be remarkably improved.
【0006】本発明での湿式造粒法は、押出し造粒、攪
はん造粒転動造粒、その他、粉体に水その他常用の結合
剤を添加し造粒する湿式造粒方法であればすべて適用で
きる。The wet granulation method according to the present invention may be extrusion granulation, stirring granulation rolling granulation, or other wet granulation method in which water or other commonly used binder is added to the powder for granulation. All are applicable.
【0007】造粒物の粒径等も特に限定はなく、目的と
する造粒乾燥品の粒径に応じて、使用する造粒機のノズ
ルやスクリーンの開口径を設定すればよい。The particle size of the granulated product is not particularly limited, and the opening diameter of the nozzle or screen of the granulator used may be set according to the particle size of the target granulated dried product.
【0008】上記造粒品は、次いで造粒品よりも大きな
開口の金網、スクリーン又はスリットを通して乾燥機に
投入される。The above granulated product is then put into a dryer through a wire net, a screen or a slit having an opening larger than that of the granulated product.
【0009】開口部の大きさは、造粒品よりも大きいこ
とが必要であるがあまりに大き過ぎても本発明の目的と
する効果が得られなくなることから、通常は、造粒品よ
りも10〜40倍程度迄の開口部であればよい。The size of the opening needs to be larger than that of the granulated product, but if it is too large, the desired effect of the present invention will not be obtained. The opening may be up to about 40 times.
【0010】湿式造粒品であっても、造粒物の粒径は一
様でなく、原料粉体の種類や造粒条件により粒度分布が
異なる。従って、通常は粒度分布中の最も大きな区分の
粒径よりも大きな開口部を有する金網、スクリーン、ス
リット等を用いる必要がある。Even in the case of a wet granulated product, the particle size of the granulated product is not uniform, and the particle size distribution varies depending on the type of raw material powder and the granulation conditions. Therefore, it is usually necessary to use a wire mesh, screen, slit or the like having an opening larger than the particle size of the largest segment in the particle size distribution.
【0011】具体的には、目的造粒物の最大粒径の2倍
ないし80倍程度の開口であればよく、100〜150
0μmの造粒物の場合乾燥前の造粒物を開口2〜20m
m程度の金網、スクリーン、スリット等を通すようにす
ればよい。Specifically, the opening may be about 2 to 80 times the maximum particle size of the target granulated product, and may be 100 to 150.
In the case of a granulated product of 0 μm, the granulated product before drying should have an opening of 2 to 20 m.
It suffices to pass a wire mesh, a screen, a slit, etc. of about m.
【0012】例えば297〜1,410μm造粒物を乾
燥後、高収率で得る方法として乾燥前の造粒物を開口
2.8〜15mm、好ましくは4〜9mmの金網、スク
リーン、スリット等を通して乾燥機に投入することによ
り、それまでの30〜40%の目的物の収率を70〜8
5%向上させることができる。For example, as a method of obtaining a high yield after drying a granulated product of 297 to 1,410 μm, the granulated product before drying is passed through a wire net, a screen, a slit or the like having an opening of 2.8 to 15 mm, preferably 4 to 9 mm. By putting it in the dryer, the yield of the desired product of 30-40% up to that time was 70-8.
It can be improved by 5%.
【0013】尚、粒度分布中で大きい方の粒径が通過し
ない開口部を用いることにより、予め好ましくない大粒
径区分を除いておき、この区分は乾燥処理せずに、回収
しリサイクルすることも可能である。By using an opening through which the larger particle size does not pass in the particle size distribution, an undesired large particle size classification is removed in advance, and this classification is collected and recycled without being dried. Is also possible.
【0014】開口部の形状は、四角、長方形、円形、楕
円形その他特に限定されない。The shape of the opening is not particularly limited to a square, a rectangle, a circle, an ellipse and the like.
【0015】金網、スクリーン、スリット等を通過した
造粒品は次いで乾燥されるが、乾燥方法に特に限定はな
く、また、乾燥後の篩分等も必要に応じ、適宜行われ
る。The granulated product that has passed through the wire mesh, screen, slits and the like is then dried, but the drying method is not particularly limited, and sieving and the like after drying is appropriately performed if necessary.
【0016】[0016]
実施例1 魚粉15%(重量%、以下同様)、食塩30%、うま味
調味料25%、糖類20%、アミノ酸10%の天然系調
味料を結合剤と共に粒径210〜1,190の範囲とな
るように攪はん造粒した。この造粒品を直接流動乾燥機
に投入すると210〜1,190μmの粒度の造粒乾燥
品が30〜40%程度しか得られなかったがこの造粒品
を4〜9mmの開口の金網またはスリットを通過させて
乾燥機に投入することで70〜90%の高収率で目的の
造粒乾燥物を得ることができる。Example 1 Fish powder 15% (weight%, the same below), salt 30%, umami seasoning 25%, sugar 20%, amino acid 10% natural seasoning with a binder in the range of particle size 210-1,190. Stir-granulated so that When this granulated product was directly put into a fluidized-bed dryer, only about 30-40% of the granulated dried product having a particle size of 210-1,190 μm was obtained, but this granulated product was wire mesh or slit with an opening of 4-9 mm. Then, the target granulated dried product can be obtained with a high yield of 70 to 90% by passing the mixture through the sol.
【0017】実施例2 野菜エキス15%、肉エキス10%、アミノ酸20%、
糖類25%、食塩30%天然系調味料を結合剤と共に転
動造粒した。この造粒品を直接流動乾燥機に投入すると
0.3〜1.5mmの粒度の目的とする造粒品が30〜
40%しか得られなかったが造粒品を5〜10mmの開
口の金網またはスリットを通過させて乾燥機に投入する
ことで70〜85%の高収率で目的の造粒乾燥物を得る
ことができた。Example 2 15% vegetable extract, 10% meat extract, 20% amino acid,
A 25% sugar and 30% salt natural seasoning was tumbled and granulated with a binder. When this granulated product is directly put into a fluidized dryer, the target granulated product having a particle size of 0.3 to 1.5 mm is 30 to 30 mm.
Although only 40% was obtained, the granulated product was passed through a wire mesh or slit having an opening of 5 to 10 mm and put into a dryer to obtain a target granulated dried product with a high yield of 70 to 85%. I was able to.
【0018】実施例3 カルシウム30%、食塩20%、アミノ酸10%、α化
米40%の食品素材の造粒において0.5〜2mmの押
し出し造粒品を2mmφのスクリーンから押し出して造
粒した物はそのまま乾燥機に投入すると60〜80%の
収率しか得られなかったが、造粒品を5〜15mmの金
網を通して乾燥機に投入することで収率を90〜95%
に向上させることができた。Example 3 In the granulation of a food material of calcium 30%, salt 20%, amino acid 10%, pregelatinized rice 40%, an extruded granule of 0.5 to 2 mm was extruded from a 2 mmφ screen to granulate. When the product was put into the drier as it was, only a yield of 60 to 80% was obtained, but by putting the granulated product into the drier through a wire net of 5 to 15 mm, the yield was 90 to 95%.
I was able to improve.
【0019】[0019]
【発明の効果】本発明方法により、湿式造粒において、
目的とする造粒乾燥物を高収率で得ることができる。According to the method of the present invention, in wet granulation,
The target granulated dried product can be obtained in high yield.
Claims (2)
粒品を乾燥機に投入する際、目的の造粒品より大きな開
口の金網、スクリーン叉はスリットを通して投入するこ
とを特徴とする造粒乾燥方法。1. In wet granulation of powder, when the granulated product is introduced into the dryer from the granulator, it is introduced through a wire mesh, a screen or a slit having a larger opening than the target granulated product. Granulation drying method.
倍の開口の金網またはスクリーン、スリットを用いるこ
とを特徴とする請求項1記載の造粒乾燥方法。2. Two to 80 times the maximum particle size of the target granulated product
The method for granulating and drying according to claim 1, wherein a wire net, a screen, or a slit having a double opening is used.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6086231A JPH07289876A (en) | 1994-04-25 | 1994-04-25 | Granulating and drying method of powder material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6086231A JPH07289876A (en) | 1994-04-25 | 1994-04-25 | Granulating and drying method of powder material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07289876A true JPH07289876A (en) | 1995-11-07 |
Family
ID=13881026
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6086231A Pending JPH07289876A (en) | 1994-04-25 | 1994-04-25 | Granulating and drying method of powder material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07289876A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012055892A (en) * | 2006-11-15 | 2012-03-22 | Zanchetta Srl | Granulation device |
JP2020162521A (en) * | 2019-03-29 | 2020-10-08 | ハウス食品株式会社 | Method for production of dry solid material |
-
1994
- 1994-04-25 JP JP6086231A patent/JPH07289876A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012055892A (en) * | 2006-11-15 | 2012-03-22 | Zanchetta Srl | Granulation device |
JP2020162521A (en) * | 2019-03-29 | 2020-10-08 | ハウス食品株式会社 | Method for production of dry solid material |
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