JP2651739B2 - Method and apparatus for sieving powders - Google Patents
Method and apparatus for sieving powdersInfo
- Publication number
- JP2651739B2 JP2651739B2 JP2169246A JP16924690A JP2651739B2 JP 2651739 B2 JP2651739 B2 JP 2651739B2 JP 2169246 A JP2169246 A JP 2169246A JP 16924690 A JP16924690 A JP 16924690A JP 2651739 B2 JP2651739 B2 JP 2651739B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- sieving
- granular material
- heat transfer
- shifter
- 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 - Fee Related
Links
Landscapes
- Combined Means For Separation Of Solids (AREA)
- Seasonings (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、小麦粉、香辛料等の粉粒体をふるい分け、
すなわち篩別する方法及び装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for sifting powders such as flour and spices,
That is, the present invention relates to a method and an apparatus for sieving.
小麦粉、香辛料等の粉粒体は、原料をロール機や高速
粉砕機等で粉砕処理して得られ、得られた粉粒体は、シ
フターで適宜篩別、分級して製品とされる。Powders and granules such as flour and spices are obtained by pulverizing raw materials with a roll machine or a high-speed pulverizer or the like, and the obtained powders and granules are appropriately sieved and classified with a shifter to obtain a product.
ところで、小麦粉、ターメリック等一部の香辛料で
は、粉砕処理の際、原料の温度が上昇し、粉砕処理後に
得られる高温の粉粒体は、結着性が高まって流動性が低
下する。従来、この粉粒体を分級するためには、上記粉
砕後の流動性が低下した粉粒体を、直接シフターに掛け
ていた。By the way, in the case of some spices such as flour and turmeric, the temperature of the raw material increases during the pulverization process, and the high-temperature powder obtained after the pulverization process has an increased binding property and a reduced fluidity. Conventionally, in order to classify the powders and granules, the powders and granules having reduced fluidity after the pulverization were directly applied to a shifter.
〔発明が解決しようとする課題〕 上記篩別において、流動性の悪い粉粒体がシフターの
目に詰って、篩別操作ができなくなる等の問題が頻発し
た。この場合、シフターの目を入替えなければならず、
手順が煩雑となり、粉粒体の品質も悪化する。また、粉
粒体の温度の低下を待って篩別を行う場合は、生産性が
低く、粉粒体の品質の面でも好ましくない。[Problems to be Solved by the Invention] In the above-mentioned sieving, problems such as sieving operation being unable to be performed due to poor flowability of the granular material clogging the eyes of the shifter frequently occurred. In this case, the eyes of the shifter must be replaced,
The procedure becomes complicated and the quality of the granular material deteriorates. Further, when sieving is performed after waiting for the temperature of the granular material to decrease, the productivity is low and the quality of the granular material is not preferable.
本発明の目的は、粉砕処理によって、結着性が高まっ
て流動性が低下した粉粒体を、シフターの目詰り等がな
く、効率的に篩別することができる、粉粒体の篩別方法
及び装置を提供することである。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for sieving powders and granules whose binding properties have been increased and flowability has been reduced by a pulverization process, without clogging of a shifter, etc. It is to provide a method and an apparatus.
本発明によれば、粉砕処理時の粉粒体の温度上昇によ
り、結着性が高まって流動性が低下した粉砕処理後の粉
粒体を、流動性がでる状態にまで冷却処理した後、篩別
することを特徴とする粉粒体の篩別方法が提供される。According to the present invention, due to a rise in the temperature of the powder during the pulverization, the powder after the pulverization, in which the binding property is increased and the fluidity is reduced, after cooling to a state where the fluidity is obtained, There is provided a method for sieving a powder, characterized by sieving.
更に、本発明によれば、本体の底部に回転軸のまわり
に攪拌部材を有する中空内部に冷却ジャケットを備えた
回転伝熱管を設け、かつ本体の側壁及び底壁に冷却ジャ
ケットを設けた冷却装置と、その下流に接続されたシフ
ターとからなる粉粒体の篩別装置が提供される。Further, according to the present invention, a cooling device in which a rotary heat transfer tube provided with a cooling jacket is provided inside a hollow having a stirring member around a rotation axis at a bottom portion of a main body, and a cooling jacket is provided on a side wall and a bottom wall of the main body. And a sifter connected downstream of the sifter.
本発明によれば、粉砕処理による粉粒体の温度上昇で
流動性が低下した粉粒体を、冷却処理及び攪拌処理によ
り、粉粒体に流動性を生じさせ、これにより熱移動速度
を増大させて効率的な冷却を図り、同時に蒸発した水分
を速やかに拡散し得る。従って、粉砕処理によって、結
着性が高まって流動性が低下した粉粒体を、シフターの
目詰り等がなく、効率的に篩別することができる。ADVANTAGE OF THE INVENTION According to this invention, the granular material which fluidity fell by the temperature rise of the granular material by a pulverization process produces fluidity in a granular material by a cooling process and a stirring process, thereby increasing a heat transfer rate. Thus, efficient cooling can be achieved, and at the same time, the evaporated water can be quickly diffused. Therefore, the pulverized material whose binding property has been increased and the fluidity has been reduced by the pulverization treatment can be efficiently sieved without clogging of the shifter or the like.
以下に本発明の実施例の粉粒体の篩別装置を図に基づ
いて説明する。第1図及び第2図に示すように、冷却装
置1は、本体2の底部に、回転軸3のまわりに攪拌部材
5を有する中空内部に冷却ジャケットを備えた回転伝熱
管4を備える。本体2は、端部に供給口9、他方の端部
に排出口10を備え、伝熱管4の形状に略合せた円弧を有
する底壁21を備える。本体2の側壁20、20′及び底壁21
は、冷却ジャケット8を備える。Hereinafter, an apparatus for sieving a granular material according to an embodiment of the present invention will be described with reference to the drawings. As shown in FIGS. 1 and 2, the cooling device 1 includes a rotary heat transfer tube 4 provided with a cooling jacket inside a hollow having a stirring member 5 around a rotary shaft 3 at the bottom of the main body 2. The main body 2 has a supply port 9 at one end, a discharge port 10 at the other end, and a bottom wall 21 having an arc approximately matching the shape of the heat transfer tube 4. Side walls 20, 20 'and bottom wall 21 of body 2
Is provided with a cooling jacket 8.
冷却媒体は、回転軸3の端部に取付けたロータリージ
ョイント6を介して伝熱管4に入り、熱伝導した後、再
びジョイント6を介して系外に出る。同様に、冷却媒体
は、冷却ジャケット8を出入する。The cooling medium enters the heat transfer tube 4 via a rotary joint 6 attached to the end of the rotating shaft 3, conducts heat, and then exits the system again via the joint 6. Similarly, the cooling medium enters and exits the cooling jacket 8.
排出口10の下流には、プランシフター等のシフター12
が設置される。Downstream of the outlet 10 is a shifter 12 such as a plan shifter.
Is installed.
粉砕処理した粉粒体は、供給口9より冷却装置1内に
供給され、回転伝熱管4で攪拌混合されながら徐々に排
出側に送られる。この間、粉粒体は、伝熱管4及び冷却
ジャケット8からの熱伝導で冷却され、流動性がよくな
るまで冷却されて排出口10から排出される。The pulverized particles are supplied from the supply port 9 into the cooling device 1 and gradually sent to the discharge side while being stirred and mixed by the rotary heat transfer tube 4. During this time, the powder is cooled by heat conduction from the heat transfer tube 4 and the cooling jacket 8, cooled until the fluidity is improved, and discharged from the outlet 10.
上記の冷却処理は、温度50〜70℃の粉砕処理後の粉粒
体が、10〜60分間以内に温度25〜35℃に冷却される条件
で行うことが望ましい。この条件は、冷却装置1を用い
る場合は、粉粒体の処理量100〜600kg/hrで、伝熱管4
及び冷却ジャケット8を合せた伝熱面積約1.5〜17m2と
することで達成できる。The above-mentioned cooling treatment is desirably performed under the condition that the granules after the pulverization treatment at a temperature of 50 to 70 ° C are cooled to a temperature of 25 to 35 ° C within 10 to 60 minutes. When the cooling device 1 is used, the conditions are as follows: the processing amount of the granular material is 100 to 600 kg / hr;
And a heat transfer area of about 1.5 to 17 m 2 including the cooling jacket 8.
冷却処理後の粉粒体は、シフター12に送られる。シフ
ター12により、例えば粒径数μm〜500μmの粉粒体か
ら、粒径150〜250μmの粉粒体を好適に篩別、分級する
ことができる。The powder or granular material after the cooling process is sent to the shifter 12. With the shifter 12, for example, a powder having a particle size of 150 to 250 μm can be suitably sieved and classified from a powder having a particle size of several μm to 500 μm.
本発明の篩別方法が適用される粉粒体は、粉砕処理時
の粉粒体の温度上昇により、結着性が高まって流動性が
低下した粉砕処理後の粉粒体であり、小麦粉、ターメリ
ック、マスタード、等の香辛料の粉粒体が例示される。
例えば、ターメリックでは、粉砕処理によって粉粒体の
温度が40〜70℃となった場合に、著しく流動性が低下
し、これを、攪拌式間接冷却装置によって流動性がでる
状態にまで冷却処理した後、篩別することにより、シフ
ターの目詰り等なしに、極めて効率的に篩別することが
できる。The granular material to which the sieving method of the present invention is applied is a granular material after the pulverization processing in which the binding property is increased and the fluidity is reduced due to an increase in the temperature of the pulverized substance during the pulverization processing. Examples include spices such as turmeric and mustard.
For example, in the case of turmeric, when the temperature of the granular material becomes 40 to 70 ° C. by the pulverization process, the fluidity is significantly reduced, and this is cooled to a state where the fluidity is obtained by the stirring type indirect cooling device. Thereafter, by sieving, sieving can be performed very efficiently without clogging of the shifter or the like.
本発明は、粉砕後の粉粒体の粒径が数μm〜500μm
であり、これらから粒径150〜250μmの粉粒体を分級す
る場合に特に有効である。また、かさ比重0.2〜0.8の粉
粒体の篩別に有効である。つまり、これらの粉粒体で
は、攪拌式間接冷却装置による攪拌、冷却効率を上げ
て、流動性のよい分級性の高いものとし、極めて効率的
に篩別することができる。本発明は、ターメリック、マ
スタード等の粉砕後に流動性の低下が著しい粉粒体の篩
別に有効である。In the present invention, the particle size of the pulverized granules is several μm to 500 μm
This is particularly effective in classifying powders having a particle size of 150 to 250 μm from these. It is also effective for sieving powders having a bulk specific gravity of 0.2 to 0.8. In other words, these particles can be sieved extremely efficiently by increasing the efficiency of stirring and cooling by the stirring type indirect cooling device to make them highly fluid and have high classifying properties. INDUSTRIAL APPLICABILITY The present invention is effective for sieving a powdery material having a remarkable decrease in fluidity after pulverizing turmeric, mustard and the like.
図示の篩別装置を用いて、粉砕処理後のターメリック
を篩別した。The turmeric after the pulverization treatment was sieved using the sieving apparatus shown.
冷却装置1は、本体2の容量約0.45m3で、φ685mmの
攪拌部材5を12基有する伝熱管4(伝熱管4及び冷却ジ
ャケット8を合せた伝熱面積約11.2m2)を備えて構成し
た。粉砕処理後のターメリック(粒径約10〜300μm、
かさ比重0.5、品温約61℃)を、供給口9より冷却装置
1に送り、500kg/hrで冷却処理した。この間、伝熱管4
を回転数20R/Mで駆動し、伝熱管4内の冷却ジャケット
及び冷却ジャケット8に20℃の冷水を約50/minで送っ
た。冷却装置1の排出口10から排出されたターメリック
は品温約29℃で、目開き250μmのプランシフター12を
通して良好に篩別することができ、篩別された粉末は香
りの良いものであった。The cooling device 1 has a capacity of about 0.45 m 3 of the main body 2 and includes a heat transfer tube 4 (a heat transfer area of about 11.2 m 2 including the heat transfer tube 4 and the cooling jacket 8) having twelve φ685 mm stirring members 5. did. Turmeric after grinding (particle size about 10-300μm,
The bulk specific gravity of 0.5 and the product temperature of about 61 ° C.) were sent from the supply port 9 to the cooling device 1 and cooled at 500 kg / hr. During this time, heat transfer tubes 4
Was driven at a rotation speed of 20 R / M, and cold water at 20 ° C. was sent to the cooling jacket and the cooling jacket 8 in the heat transfer tube 4 at about 50 / min. The turmeric discharged from the outlet 10 of the cooling device 1 was able to be sifted through a plan shifter 12 having an opening of 250 μm at a product temperature of about 29 ° C., and the sieved powder had a good aroma. .
本発明によると、粉砕処理による粉粒体の温度上昇で
流動性が低下した粉粒体を、攪拌式間接冷却装置によっ
て冷却処理することにより、同冷却装置の回転伝熱面の
攪拌効果により、粉粒体に流動性を生じさせ、これによ
り熱移動速度を増大させて効率的な冷却を図り、同時に
蒸発した水分の拡散が速やかに行い得る。従って、粉砕
処理によって、結着性が高まって流動性が低下した粉粒
体を、シフターの目詰り等がなく、効率的に篩別するこ
とができる。According to the present invention, by cooling the granular material whose fluidity has decreased due to the temperature rise of the granular material by the pulverizing process by the stirring type indirect cooling device, by the stirring effect of the rotary heat transfer surface of the cooling device, Fluidity is generated in the granular material, thereby increasing the heat transfer rate to achieve efficient cooling, and at the same time, quickly diffuse the evaporated water. Therefore, the pulverized material whose binding property has been increased and the fluidity has been reduced by the pulverization treatment can be efficiently sieved without clogging of the shifter or the like.
第1図は本発明による篩別装置の全体を示す斜視図、 第2図は本発明による篩別装置のA1−A2面における断面
図を示す。 1……冷却装置、 2……本体、 3……中空回転軸、 4……回転伝熱管、 5……攪拌部材、 6……ロータリージョイント、 8……冷却ジャケット、 9……供給口、 10……排出口、 12……シフター、 20、20′……側壁、 21……底壁。Perspective view of an entire sieve means according to Figure 1 the present invention, Figure 2 is a cross sectional view taken along A 1 -A 2 side of the sieve means according to the present invention. DESCRIPTION OF SYMBOLS 1 ... Cooling device, 2 ... Body, 3 ... Hollow rotating shaft, 4 ... Rotary heat transfer tube, 5 ... Stirring member, 6 ... Rotary joint, 8 ... Cooling jacket, 9 ... Supply port, 10 ... outlet, 12 ... shifter, 20, 20 '... side wall, 21 ... bottom wall.
Claims (4)
着性が高まって流動性が低下した粉砕処理後の粉粒体
を、流動性がでる状態にまで冷却処理した後、篩別する
ことを特徴とする粉粒体の篩別方法。1. A method comprising the steps of: cooling a powdery material having a reduced fluidity due to an increase in binding property due to a rise in the temperature of the powdery material during the pulverization process until the powdery material is cooled; A method for sieving a granular material, comprising:
う請求項1記載の方法。2. The method according to claim 1, wherein the cooling treatment is performed by a stirring type indirect cooling device.
又は2記載の方法。3. The turmeric powder according to claim 1, wherein the powder is turmeric.
Or the method of 2.
に攪拌部材(5)を有する中空内部に冷却ジャケットを
備えた回転伝熱管(4)を設け、かつ本体(2)の側壁
(20、20′)及び底壁(21)に冷却ジャケット(8)を
設けた冷却装置(1)と、その下流に接続されたシフタ
ー(12)とからなる粉粒体の篩別装置。4. A rotary heat transfer tube (4) having a cooling jacket in a hollow interior having a stirring member (5) around a rotation axis (3) at the bottom of the main body (2), and A sieving apparatus for a granular material, comprising: a cooling device (1) provided with a cooling jacket (8) on a side wall (20, 20 ') and a bottom wall (21); and a shifter (12) connected downstream thereof.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2169246A JP2651739B2 (en) | 1990-06-27 | 1990-06-27 | Method and apparatus for sieving powders |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2169246A JP2651739B2 (en) | 1990-06-27 | 1990-06-27 | Method and apparatus for sieving powders |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0461972A JPH0461972A (en) | 1992-02-27 |
JP2651739B2 true JP2651739B2 (en) | 1997-09-10 |
Family
ID=15882954
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2169246A Expired - Fee Related JP2651739B2 (en) | 1990-06-27 | 1990-06-27 | Method and apparatus for sieving powders |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2651739B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103416707B (en) * | 2013-08-07 | 2015-04-29 | 苏州闻达食品配料有限公司 | Ground spice temperature return device |
-
1990
- 1990-06-27 JP JP2169246A patent/JP2651739B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0461972A (en) | 1992-02-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3541693B2 (en) | Crushing and sizing device for powders and granules | |
JPH09108585A (en) | Device for disintegrating and granulating granular material and annular space type screen | |
JP2651739B2 (en) | Method and apparatus for sieving powders | |
JP2750325B2 (en) | Crushing and sizing machine | |
JP2804415B2 (en) | Apparatus and method for wetting and dissolving dry particles | |
JPH0827133B2 (en) | Wet powder processing equipment | |
JP2000302716A (en) | Production of granular phenols | |
JPH05236A (en) | Stirring granulator | |
CN214390560U (en) | Preparation facilities of medicinal lauryl sodium sulfate fine powder | |
JPH0678711A (en) | Production of granular dipeptide sweetener | |
JP6289981B2 (en) | Dispersing mechanism of workpiece in airflow dryer | |
JP4287732B2 (en) | Powder and granulator | |
HU185004B (en) | Process for separating dry substant content of solutions and/or suspensions and in forme of granulate, and for granulating powders and mixtures of powders in a layer fluidized with gas, and apparatus for the process | |
JP2985341B2 (en) | Granulation equipment for metal powder production | |
JPH11114442A (en) | Apparatus for producing crushed sand | |
JPH10338518A (en) | Production of calcium carbonate | |
JP3234162B2 (en) | Granulator | |
CN210346225U (en) | Drying device for combined use of airflow drying system and horizontal boiling cooler | |
JPH10114709A (en) | Production of particulate neopentyl glycol hydroxypivalate, particle produced thereby and granulation of the particle with granulator | |
JPH06297197A (en) | Method and device for dry granulation | |
JPH0519072B2 (en) | ||
JPH10318673A (en) | Method and apparatus for drying powder particles | |
JP3228288B1 (en) | Method for producing pharmaceutical granule preparation containing branched chain amino acids | |
JPS6398372A (en) | Production of granular food | |
CN112473998A (en) | Preparation device and method of medicinal lauryl sodium sulfate fine powder |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080523 Year of fee payment: 11 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090523 Year of fee payment: 12 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090523 Year of fee payment: 12 |
|
FPAY | Renewal fee payment (prs date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100523 Year of fee payment: 13 |
|
LAPS | Cancellation because of no payment of annual fees |