JPH07159034A - Dryer for wet food and the like - Google Patents

Dryer for wet food and the like

Info

Publication number
JPH07159034A
JPH07159034A JP5329549A JP32954993A JPH07159034A JP H07159034 A JPH07159034 A JP H07159034A JP 5329549 A JP5329549 A JP 5329549A JP 32954993 A JP32954993 A JP 32954993A JP H07159034 A JPH07159034 A JP H07159034A
Authority
JP
Japan
Prior art keywords
raw material
drying
cylinder
blower
partition plate
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
JP5329549A
Other languages
Japanese (ja)
Other versions
JP2869515B2 (en
Inventor
Hiromi Kawachi
博美 河内
Minoru Ooka
稔 大岡
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.)
Tokyo Rope Manufacturing Co Ltd
Tokyo Seiko Co Ltd
Original Assignee
Tokyo Rope Manufacturing Co Ltd
Tokyo Seiko 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 Tokyo Rope Manufacturing Co Ltd, Tokyo Seiko Co Ltd filed Critical Tokyo Rope Manufacturing Co Ltd
Priority to JP5329549A priority Critical patent/JP2869515B2/en
Publication of JPH07159034A publication Critical patent/JPH07159034A/en
Application granted granted Critical
Publication of JP2869515B2 publication Critical patent/JP2869515B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/85Food storage or conservation, e.g. cooling or drying

Abstract

PURPOSE:To improve drying performance, reliability by repeatedly granulating and heating raw material to enhance fluidity and a heat exchanging efficiency and dry uniformly. CONSTITUTION:The dryer for food and the like comprises a screw feeder 3 connected to a lower part of a drying cylinder 1 and a raw material supply hopper 2 to receive and feed supplying or drying raw material (a), a blower 5 connected to the feeder 3 to feed under pressure the material (a) together with input gas and hot gas, and a circulating cylinder 6 connected to the blower 5 to feed the material (a) to diffuse it into a ceiling 11 in the cylinder 1. Further, the dryer comprises a plurality of stages of partition plates 12 with dropping holes arranged in the cylinder 1, heating means 20 attached to the plates 12, and agitating scrapers 15 arranged on the plates 12.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、豆腐製造時の残滓(オ
カラ)や各種の野菜、魚介類の廃棄物等を乾燥する湿潤
食品類の乾燥装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a drier for damp foods, which dries residue (okara), various vegetables and wastes of seafood during tofu production.

【0002】[0002]

【従来の技術】豆腐製造時にできる大量の残滓(オカ
ラ)は、そのまま食品等として直接に利用する消費量は
少なくその大多数が廃棄されているが、含水90%以上
の高湿潤粉粒物で嵩高、重量物であり、その取扱いや廃
棄に多くの手数、手間を要するため、この残滓(オカ
ラ)を乾燥処理して軽量とし袋詰め保管等を容易にし
て、動植物の飼料や肥料等に有効利用することが提案さ
れている。例えば、解砕機でその残滓(オカラ)を解き
ほぐして流動性を高め、熱風とともに複数連の遠赤外線
乾燥管内を流通せしめ、遠赤外線を放射して乾燥する湿
潤食品類の乾燥装置が開発されている。
2. Description of the Related Art A large amount of residue (okara) produced during the production of tofu is directly consumed as food, etc., and the majority of it is discarded, but it is a highly moist powder with a water content of 90% or more. Since it is bulky and heavy, and it requires a lot of labor and time to handle and dispose of it, this residue (okara) is dried to make it lightweight and easy to store in bags, and it is effective for animal and plant feed and fertilizer. Proposed to be used. For example, a drier for wet foods has been developed, which uses a crusher to loosen the residue (okara) to improve fluidity and to let it flow in a series of far infrared ray drying tubes together with hot air, and emit far infrared rays to dry it. .

【0003】[0003]

【発明が解決しようとする課題】従来の湿潤食品類の乾
燥装置は、前記の残滓(オカラ)のような高湿潤粉粒物
を乾燥する場合、前記のような解砕機による一度の解き
ほぐし程度ではその細粒化に限界があり、熱風を多量に
混入させて流動性を付与して流通せしめる必要があり、
熱交換効率や処理能率が低下し乾燥のバラツキが生じ易
く、また、装置が大型化しイニシアルコストが増加する
などの課題がある。
A conventional drying apparatus for wet foods, when drying a highly wet powdery substance such as the above-mentioned residue (okara), does not have to be loosened once by a crusher as described above. There is a limit to the atomization, it is necessary to mix a large amount of hot air to impart fluidity and distribute it,
There are problems that the heat exchange efficiency and the processing efficiency are lowered, and the dispersion of the drying is apt to occur, and that the apparatus becomes large and the initial cost increases.

【0004】本発明は、上記のような課題に対処するた
めに開発されたものであつて、その目的とする処は、原
料の細粒化及び加熱を繰り返して流動性とともに熱交換
効率を高め乾燥を均等化して乾燥性能、信頼性を向上し
た湿潤食品類の乾燥装置を提供するにある。
The present invention was developed in order to address the above-mentioned problems. The object of the present invention is to improve the fluidity and heat exchange efficiency by repeating atomization and heating of the raw material. An object is to provide a drying device for wet foods, which has uniform drying and improved drying performance and reliability.

【0005】[0005]

【課題を解決するための手段】本発明は、乾燥筒及び原
料供給ホツパーの下部に連設され供給又は乾燥中の原料
を受けて移送するスクリュウフイーダーと、スクリュウ
フイーダーに連設され入気や熱気とともに原料を圧送す
るブロワーと、ブロワーに連設され原料を移送して乾燥
筒内の天井に吹き付ける循環筒と、乾燥筒内に配設した
複数段の落下穴付き仕切板と、仕切板に付設した加熱手
段と、前記の各仕切板上に配設した攪拌兼スクレーパー
を具備したことにより、原料の細粒化を繰り返して流動
性とともに熱交換効率を高め、かつ乾燥を均等化して急
速に乾燥処理される。
DISCLOSURE OF THE INVENTION The present invention is directed to a screw feeder which is connected to a lower portion of a drying cylinder and a material supply hopper and which receives and transfers a material being supplied or dried, and an air intake member which is connected to the screw feeder. And a blower that sends the raw material under pressure with hot air, a circulation tube that is connected to the blower to transfer the raw material and blows it onto the ceiling of the drying cylinder, a partition plate with multiple drop holes arranged in the drying cylinder, and a partition plate By providing a heating means attached to the above and a stirring and scraper arranged on each of the above-mentioned partition plates, it is possible to improve the fluidity and heat exchange efficiency by repeating the atomization of the raw material, and to even out the drying process to achieve rapid drying. Is dried.

【0006】[0006]

【作用】原料供給ホツパーから供給される原料は、スク
リュウフイーダーによりブロワーに移送され、ブロワー
と循環筒により入気や熱気とともに攪拌、圧送されて乾
燥筒内の天井に吹き付けられ、その積極的な衝突、飛散
により効果的に細粒化及び分散するとともに、最上段の
仕切板及び攪拌兼スクレーパーによりさらに攪拌・旋回
及び加熱され効率良く一次乾燥された後、落下して同様
な乾燥が複数回繰り返えされ、さらに循環により前記の
移送、乾燥を連続的に繰り返えし円滑に遂行され、原料
が効果的に細粒化されて流動性とともに熱交換効率が著
しく高められ、かつ乾燥が均等化されて急速に乾燥さ
れ、優れた乾燥処理性能、信頼性が得られる。
[Function] The raw material supplied from the raw material supply hopper is transferred to the blower by the screw feeder, and is agitated and pressure-fed with the intake air and hot air by the blower and the circulation cylinder and sprayed to the ceiling in the drying cylinder, The particles are effectively atomized and dispersed by collision and scattering, and are further agitated and swirled and heated by the uppermost partition plate and agitation / scraper to be efficiently primary dried, and then dropped to repeat similar drying several times. It is returned, and the transfer and drying are continuously repeated by circulation to be smoothly performed, and the raw material is effectively atomized to improve the fluidity and the heat exchange efficiency, and the drying is even. It is liquefied and dried rapidly, resulting in excellent dry processing performance and reliability.

【0007】[0007]

【実施例】図1及び図2に本発明の一実施例を示す。図
中1は乾燥筒、2は乾燥処理する原料aの原料供給ホツ
パー、3は供給又は乾燥中の原料aのスクリュウフイー
ダー、5は原料を高速で圧送する攪拌兼用のブロワー、
6はブロワーと乾燥筒1の上部に連設した循環筒、8は
循環筒の中途に切換えダンパー7を介し分岐した乾燥製
品の排出筒、11は乾燥筒1内の天井、12は乾燥筒内
に配設した複数段の落下穴14付き仕切板、15は各仕
切板上に配設した攪拌兼スクレーパー、20は仕切板の
加熱手段、24は排気口、25は乾燥筒1の下部に配設
した循環用シユート、26は駆動用の減速機27付きモ
ーター、aは乾燥する原料(湿潤食品類)、b〜jは原
料の移動経路であり、図示の実施例は、乾燥筒1及び原
料供給ホツパー2の下部に連設され供給又は乾燥中の原
料aを受けて移送するスクリュウフイーダー3と、スク
リュウフイーダーに連設され入気や熱気とともに原料a
を圧送するブロワー5と、ブロワーに連設され原料aを
移送して乾燥筒1内の天井11に吹き付ける循環筒6
と、乾燥筒内に配設した複数段の落下穴14付き仕切板
12と、仕切板に付設した加熱手段20と、各仕切板上
に配設した攪拌兼スクレーパー15を具備した湿潤食品
類の乾燥装置になつている。
1 and 2 show an embodiment of the present invention. In the drawing, 1 is a drying cylinder, 2 is a raw material supply hopper for the raw material a to be dried, 3 is a screw feeder for the raw material a being supplied or being dried, 5 is a blower that also serves as a stirrer for pressure-feeding the raw material,
Reference numeral 6 denotes a blower and a circulation cylinder connected to the upper part of the drying cylinder 1, 8 denotes a dry product discharge cylinder branched through a switching damper 7 in the middle of the circulation cylinder, 11 denotes a ceiling inside the dry cylinder 1, and 12 denotes inside the dry cylinder. A partition plate with a plurality of stages of falling holes 14 disposed therein, 15 an agitator / scraper disposed on each partition plate, 20 heating means for the partition plate, 24 an exhaust port, and 25 a lower part of the drying cylinder 1. A circulating shout provided, 26 is a motor with a speed reducer 27 for driving, a is a raw material (wet foods) to be dried, b to j are movement paths of the raw material, and in the illustrated embodiment, the drying cylinder 1 and the raw material are used. A screw feeder 3 that is connected to the lower part of the supply hopper 2 and receives and transfers the raw material a that is being supplied or dried, and a raw material a that is connected to the screw feeder and that is connected to the screw feeder and that has intake air or hot air.
Blower 5 for pressure-feeding, and circulation cylinder 6 connected to the blower for transferring raw material a and spraying it on ceiling 11 in drying cylinder 1.
A partition plate 12 having a plurality of stages of falling holes 14 arranged in a drying cylinder, a heating means 20 attached to the partition plate, and a stirrer / scraper 15 arranged on each partition plate. It is a drying device.

【0008】さらに詳述すると、図示の湿潤食品類の乾
燥装置は、図1(B)に示すような制御盤30、コント
ローラ31及び制御手段32a〜32e等からなる駆動
制御機構を有し、乾燥処理する湿潤食品類の種類や粉粒
度、湿潤度等のデータに基づく各種の制御パターンが予
め入力され、制御盤30を操作すると、湿潤食品類に対
応した制御パターンの制御信号30a,31aが出力さ
れ、モーター26の動力伝達系において、各制御手段3
2a〜32eによりスクリュウフイーダー3、ブロワー
5、攪拌兼スクレーパー15、加熱手段20や切換えダ
ンパー7が駆動制御される(マニユアル操作手段も併
設、図示省略)。
More specifically, the illustrated drying apparatus for wet foods has a drive control mechanism including a control panel 30, a controller 31, and control means 32a to 32e as shown in FIG. Various control patterns based on data such as types of wet foods to be processed, powder particle size, and degree of wetness are input in advance, and when the control panel 30 is operated, control signals 30a and 31a having control patterns corresponding to wet foods are output. In the power transmission system of the motor 26, each control means 3
The screw feeder 3, the blower 5, the stirring and scraper 15, the heating means 20 and the switching damper 7 are drive-controlled by 2a to 32e (manual operating means is also provided, not shown).

【0009】例えば、豆腐製造時の残滓(オカラ)を乾
燥対象の原料aとする場合、制御盤30を操作すると、
モータ26が作動し、原料aに対応した制御パターンの
制御信号30a,31aが出力されて、各制御手段32
a〜32eにより乾燥装置の各部が一連に駆動制御され
る。即ち、スクリュウフイーダー3は、乾燥筒1下部の
循環用シユート25及びバルブ2a付き原料供給ホツパ
ー2の下側に連設されて、制御手段32aを介し回転制
御されて、原料供給ホツパー2から供給され又は循環用
シユート25から循環される乾燥中の原料aを、入気
(原料供給ホツパー2から)や熱気(乾燥筒1から)と
ともに制御された速度でブロワー5に円滑に移送する
(矢示方向b)。
For example, when the residue (okara) at the time of tofu production is used as the raw material a to be dried, when the control panel 30 is operated,
The motor 26 operates and the control signals 30a and 31a of the control pattern corresponding to the raw material a are output, and the control means 32 are provided.
Each part of the drying device is sequentially driven and controlled by a to 32e. That is, the screw feeder 3 is connected to the lower side of the raw material supply hopper 2 with the circulation shout 25 and the valve 2a at the lower part of the drying cylinder 1, and is rotationally controlled by the control means 32a to supply from the raw material supply hopper 2. The raw material a being dried or circulated from the circulation short 25 is smoothly transferred to the blower 5 at a controlled speed together with the intake air (from the raw material supply hopper 2) and the hot air (from the drying cylinder 1) (arrow direction). Direction b).

【0010】ブロワー5は、回転方向に対し適度の後傾
角(53度程度)で斜設された複数のブレード5aを有
し、制御手段32bを介し回転制御されて、各ブレード
5aにより原料aを適度に攪拌して入気や熱気とともに
所定の高速で循環筒6に圧送し(矢示方向c)、循環筒
6は、その上、下端部がブロワー5と乾燥筒1の上壁部
に連通され、ブロワー5から送り込まれる原料aを入気
や熱気とともに高速で移送し(矢示方向d)、その上端
部6aから乾燥筒1内の天井11に広く矢示方向eに吹
き付けかつ適度の旋回流にして、原料aを衝突、飛散せ
しめ積極的に細粒化して均等に分散する。
The blower 5 has a plurality of blades 5a obliquely installed at an appropriate rearward inclination angle (about 53 degrees) with respect to the rotation direction, and the rotation of the blades 5a is controlled by the control means 32b. The mixture is appropriately stirred and pressure-fed with the intake air and the hot air to the circulation cylinder 6 at a predetermined high speed (arrow direction c), and the circulation cylinder 6 has its upper and lower ends communicating with the blower 5 and the upper wall of the drying cylinder 1. The raw material a sent from the blower 5 is transferred at high speed together with the intake air and the hot air (arrow direction d), and is sprayed from the upper end portion 6a thereof to the ceiling 11 in the drying cylinder 1 widely in the arrow direction e and swirled appropriately. Then, the raw material a is collided and scattered to be positively atomized and uniformly dispersed.

【0011】乾燥筒1は、周囲に断熱層(空間、必要に
応じ断熱材を充填)1a及び上部に排気口24を有し、
その内部に吹き付けられる原料aを飛散する天井11
や、仕切板12及び攪拌兼スクレーパー15を複数段に
配設し、下部に循環用シユート25とスクリュウフイー
ダー2を配設している。その各仕切板12は、図示のよ
うに乾燥筒1内を上下間隔を置き複数段に仕切り、その
内部に形成した温水循環室13に加熱手段20(温水発
生器21、流入口22a及び流出口22b付き温水配管
22等)を付設し、制御手段32cを介しその温水発生
器21を制御(水温、流量)して、その加熱水を矢示方
向に循環制御し各仕切板12の温水循環室13内に流通
せしめ原料aを熱気とともに適温で加熱するホツトプレ
ート機構とし、各仕切板12には原料aの落下穴14を
配設している(図2参照)。また、攪拌兼スクレーパー
15は、各仕切板12上に配設され、共通の駆動軸16
で回転制御される攪拌バー17とスクレーパー18を有
し、制御手段32dを介し回転制御されて、仕切板12
上の原料aを攪拌バー17で適度に攪拌及び移送し、ス
クレーパー18で移送して矢示方向gに旋回せしめ加熱
乾燥して、落下穴14から次段に落下hせしめ、原料a
の攪拌、旋回及び加熱乾燥を複数回(図示例は3回)繰
り返した後、この乾燥中の原料aを熱気とともに循環用
シユート25から再びスクリュウフイーダー2に送り込
み循環し、前記の工程を連続的に繰り返し反復して乾燥
する構造になつている。
The drying cylinder 1 has a heat insulating layer (a space, if necessary filled with a heat insulating material) 1a in the periphery and an exhaust port 24 in the upper portion,
Ceiling 11 that scatters raw material a sprayed inside
Alternatively, the partition plate 12 and the agitator / scraper 15 are arranged in a plurality of stages, and the circulation shout 25 and the screw feeder 2 are arranged below. As shown in the figure, each partition plate 12 partitions the inside of the drying cylinder 1 into a plurality of stages at upper and lower intervals, and a heating means 20 (a warm water generator 21, an inflow port 22a and an outflow port) is provided in a hot water circulation chamber 13 formed therein. Hot water pipe 22 with 22b) is attached, the hot water generator 21 is controlled (water temperature, flow rate) via the control means 32c, and the heated water is circulated in the direction of the arrow to control the hot water circulation chamber of each partition plate 12. A hot plate mechanism that heats the raw material a by circulating it in the inside 13 together with hot air is provided, and a drop hole 14 for the raw material a is provided in each partition plate 12 (see FIG. 2). The stirring and scraper 15 is disposed on each partition plate 12 and has a common drive shaft 16
It has a stirring bar 17 and a scraper 18 which are rotationally controlled by the partition plate 12 which is rotationally controlled by a control means 32d.
The above material a is appropriately stirred and transferred by a stirring bar 17, transferred by a scraper 18, swirled in a direction g as indicated by an arrow, heated and dried, and then dropped h from a drop hole 14 to the next stage.
After repeating the stirring, swirling, and heat drying a plurality of times (three times in the illustrated example), the raw material a being dried is sent together with hot air from the circulation shout 25 to the screw feeder 2 for circulation, and the above steps are continued. It has a structure that it is repeatedly and repeatedly dried.

【0012】前記の乾燥筒1において、原料aは、循環
筒6の上端部6aから高速で乾燥筒1内の天井11に向
かって矢示方向eに吹き付けられ、図示のように少し偏
向流にて天井11に広く衝突されかつ適度の旋回流とな
つて矢示方向fに飛散され、その衝突により積極的に細
粒化、分散されるとともに、さらに、最上段の仕切板1
2上で回転駆動する攪拌兼スクレーパー15で適度の攪
拌を受けて旋回流gとなり、仕切板12の温水循環室1
3内の加熱水で加熱され一次乾燥されて落下穴14から
次段に落下し(矢示方向h)、最上段の仕切板12上で
効率良く熱交換されて乾燥される、続いて、次段さらに
最下段の仕切板12及び攪拌兼スクレーパー15で同様
な二次乾燥、三次乾燥が繰り返された後、循環用シユー
ト25から再びスクリュウフイーダー3に送り込まれて
循環され前記の乾燥が連続して繰り返えされる。また、
前記の乾燥中、乾燥筒1の上部に設けた排気口24から
熱気が適量排出され、それに伴い原料供給ホツパー2か
ら入気されて補われ、熱気の交換が適度に行われて移送
とともに加熱乾燥が円滑に遂行される。
In the drying cylinder 1, the raw material a is sprayed at a high speed from the upper end portion 6a of the circulation cylinder 6 toward the ceiling 11 in the drying cylinder 1 in the direction e as shown by the arrow, and is slightly deflected as shown in the figure. Is widely collided with the ceiling 11 and is scattered in the direction f of the arrow in the form of an appropriate swirling flow, and the collision causes the particles to be finely divided and dispersed, and further, the uppermost partition plate 1
The stirring and scraper 15 which is rotationally driven on 2 receives a proper amount of stirring to generate a swirling flow g, and the hot water circulation chamber 1 of the partition plate 12
It is heated by the heated water in 3 to be primarily dried and then dropped to the next stage from the drop hole 14 (direction h in the arrow direction), and is efficiently heat-exchanged and dried on the uppermost partition plate 12, and then the next. The same secondary drying and tertiary drying are repeated by the partition plate 12 and the agitator / scraper 15 at the lowermost stage, and then sent from the circulation shout 25 to the screw feeder 3 again to be circulated and continuously dried. Is repeated. Also,
During the above-mentioned drying, an appropriate amount of hot air is discharged from the exhaust port 24 provided in the upper part of the drying cylinder 1, and accordingly, the raw material supply hopper 2 is introduced to supplement the hot air, and the hot air is appropriately exchanged and heated and dried together with the transfer. Is carried out smoothly.

【0013】原料aの乾燥程度は、例えば、排気口24
に配設したセンサー(図示省略)等による排気の湿度検
出等で容易に判断され、その検出信号に基づく制御手段
32eの制御により循環筒6の中途に設けた切換えダン
パー7が点線のように切り換えられて、その乾燥製品
は、循環筒6の中途に分岐した排出筒8により取り出し
て容器29に受け取られる。なお、手操作による操作手
段も併設されており(図示省略)、例えば、乾燥筒1の
側部に設けた覗き窓により内部の原料aの飛散状態を観
察して、その乾燥度を察知し切換えダンパー7を切り換
える手操作も可能である(図示省略)。
The degree of drying of the raw material a is, for example, the exhaust port 24.
It is easily judged by detecting the humidity of the exhaust gas by a sensor (not shown) provided in the above, and the switching damper 7 provided in the middle of the circulation cylinder 6 is switched as indicated by the dotted line by the control of the control means 32e based on the detection signal. Then, the dried product is taken out by the discharge tube 8 branched in the middle of the circulation tube 6 and received in the container 29. A manual operation means is also provided (not shown). For example, the scattering state of the raw material a inside is observed through a viewing window provided on the side of the drying cylinder 1, and the degree of dryness thereof is detected to switch. Manual operation for switching the damper 7 is also possible (not shown).

【0014】前記のように、原料aは、ブロワー5によ
る攪拌及び圧送、循環筒による乾燥筒6内の天井11へ
の吹き付け飛散、続いて、複数段の仕切板12及び攪拌
兼スクレーパー15による適度の攪拌及び旋回、加熱乾
燥の繰り返し、さらに循環による繰り返しで連続乾燥さ
れる。前記の残滓(オカラ)のように極めて高湿潤の食
品類であつても、前記のような細粒化及び加熱乾燥の繰
り返しにより円滑に移送されるとともに、熱交換効率が
著しく高められて素早く乾燥処理される。
As described above, the raw material a is agitated and pressure-fed by the blower 5, sprayed and scattered to the ceiling 11 in the drying cylinder 6 by the circulation cylinder, and then appropriately divided by the plurality of partition plates 12 and the agitation / scraper 15. The continuous drying is carried out by repeating the stirring and swirling, the heating and drying, and the circulation. Even extremely high-humidity foods such as the above-mentioned residue (okara) can be smoothly transferred by repeating the above-mentioned granulation and heat drying, and the heat exchange efficiency can be remarkably enhanced to dry quickly. It is processed.

【0015】図示のように仕切板12及び攪拌兼スクレ
ーパー15を3段に配設した乾燥装置によつて、オカラ
(含水90%)を48kg投入して乾燥した結果、約2
0分で十分に乾燥された乾燥製品が得られた。従来の乾
燥機に比べ10分程度早く乾燥処理される。また、この
乾燥処理を毎日繰り返しても電機代/月は2万円程とな
り大幅に節減された。即ち、装置が著しく小型化されて
低コストで提供され、イニシヤルコストが著しく節減さ
れる。
As shown in the figure, 48 kg of okara (water content: 90%) was put into a drying device having a partition plate 12 and a stirring / scraper 15 arranged in three stages, and the result was about 2
A fully dried product was obtained in 0 minutes. It is dried about 10 minutes earlier than conventional dryers. Even if this drying process was repeated every day, the electricity bill / month was about 20,000 yen, which was a significant reduction. That is, the device is significantly downsized and provided at a low cost, and the initial cost is significantly reduced.

【0016】前記の実施例では、主として豆腐製造時に
できる残滓(オカラ)の乾燥処理について説明したが、
多量の水分を含有する各種の魚介等の廃棄物についても
同様に適用される。なお、これらの廃棄物は必要に応じ
粉砕機(図示省略)で予め粉砕して乾燥処理される。ま
た、加熱手段は、図示の加熱水に代えて熱気によること
もでき多様な機構に設計される。前記の乾燥装置は、乾
燥処理される原料の種類、処理量等に対応した乾燥筒の
サイズや仕切板及び攪拌兼スクレーパーの段数に設計さ
れる。
In the above-mentioned embodiment, the drying treatment of the residue (okara) which is mainly produced during the production of tofu has been explained.
The same applies to wastes such as various seafood containing a large amount of water. If necessary, these wastes are pulverized by a pulverizer (not shown) and dried. Further, the heating means may be hot air instead of the illustrated heated water and is designed in various mechanisms. The above-mentioned drying device is designed in the size of the drying cylinder corresponding to the type of raw material to be dried, the amount of treatment, etc., the number of partitions and the number of stages of the agitation and scraper.

【0017】[0017]

【発明の効果】本発明は、前述のように構成され原料供
給ホツパーから供給される原料は、スクリュウフイーダ
ーによりブロワーに移送され、ブロワーと循環筒により
入気や熱気とともに攪拌、圧送されて、乾燥筒内の天井
に吹き付けられ積極的に衝突、飛散されて効果的に細粒
化及び分散されるとともに、最上段の仕切板及び攪拌兼
スクレーパーにより攪拌、旋回され効率良く加熱されて
一次乾燥された後、落下して同様に二次乾燥、三次乾燥
され、再び循環されて前記の移送、乾燥が連続的に繰り
返し反復されて、その原料が効果的に細粒化されて流動
性とともに熱交換効率が著しく高められ、乾燥が均等化
されて急速に乾燥処理され処理能率が著しく高められる
など、乾燥処理性能、信頼性が著しく向上されている。
According to the present invention, the raw material supplied from the raw material supply hopper constructed as described above is transferred to the blower by the screw feeder, and is agitated and pumped together with the intake air and the hot air by the blower and the circulation cylinder, It is sprayed on the ceiling in the drying cylinder and is positively collided and scattered to be effectively granulated and dispersed, and is also agitated and swirled by the uppermost partition plate and agitation and scraper to be efficiently heated and primary dried. After that, it is dropped and similarly subjected to secondary drying and tertiary drying, and is circulated again to repeat the above-mentioned transfer and drying continuously and repeatedly, and the raw material is effectively granulated, and heat exchange is performed together with fluidity. Drying performance and reliability are remarkably improved, for example, the efficiency is remarkably increased, the drying is made uniform, and the drying treatment is rapidly performed to remarkably improve the treatment efficiency.

【0018】従ってまた、装置の小形化が可能となり低
コストで提供され、イニシヤルコストが節減されるなど
の利点を有する。
Therefore, there is an advantage that the device can be downsized and provided at low cost, and the initial cost can be reduced.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例を示す縦断機構図(A)とそ
の制御ブロツク図(B)
FIG. 1 is a longitudinal sectional view (A) and a control block diagram thereof (B) showing an embodiment of the present invention.

【図2】図1のX−X部分の横断面図である。FIG. 2 is a cross-sectional view taken along the line XX of FIG.

【符号の説明】[Explanation of symbols]

1 乾燥筒 2 原料供給ホツパー 3 スクリュウフイーダー 5 ブロワー 6 循環筒 11 天井 12 仕切板 14 落下穴 15 攪拌兼スクレーパー 20 加熱手段 a 原料(湿潤食品類) 1 Drying Cylinder 2 Raw Material Supply Hopper 3 Screw Feeder 5 Blower 6 Circulation Cylinder 11 Ceiling 12 Partition Plate 14 Falling Hole 15 Stirring and Scraper 20 Heating Means a Raw Material (wet foods)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 乾燥筒及び原料供給ホツパーの下部に連
設され供給又は乾燥中の原料を受けて移送するスクリュ
ウフイーダーと、同スクリュウフイーダフイーダーに連
設され入気や熱気とともに原料を圧送するブロワーと、
同ブロワーに連設され原料を移送して乾燥筒内の天井に
吹き付ける循環筒と、同乾燥筒内に配設した複数段の落
下穴付き仕切板と、同仕切板に付設した加熱手段と、前
記の各仕切板上に配設した攪拌兼スクレーパーを具備し
たことを特徴とする湿潤食品類の乾燥装置。
1. A screw feeder connected to a lower portion of a drying cylinder and a raw material supply hopper and configured to receive and transfer a raw material being supplied or dried, and a screw feeder connected to the screw feeder to feed the raw material together with intake air and hot air. With a blower
A circulation tube connected to the blower to transfer the raw material and blow it onto the ceiling in the drying tube, a partition plate with a plurality of stages of falling holes arranged in the drying tube, and heating means attached to the partition plate, A drier for wet foods, comprising a stirrer / scraper arranged on each of the partition plates.
JP5329549A 1993-12-02 1993-12-02 Drying equipment for wet foods Expired - Lifetime JP2869515B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5329549A JP2869515B2 (en) 1993-12-02 1993-12-02 Drying equipment for wet foods

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5329549A JP2869515B2 (en) 1993-12-02 1993-12-02 Drying equipment for wet foods

Publications (2)

Publication Number Publication Date
JPH07159034A true JPH07159034A (en) 1995-06-20
JP2869515B2 JP2869515B2 (en) 1999-03-10

Family

ID=18222605

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5329549A Expired - Lifetime JP2869515B2 (en) 1993-12-02 1993-12-02 Drying equipment for wet foods

Country Status (1)

Country Link
JP (1) JP2869515B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100233231B1 (en) * 1997-07-25 1999-12-01 정학철 Process device for food garbage
JP2006166805A (en) * 2004-12-16 2006-06-29 Mayekawa Mfg Co Ltd Method and apparatus for freezing, cooling and heating granule or the like
WO2012011600A1 (en) * 2010-07-23 2012-01-26 北海道特殊飼料株式会社 Drying device and drying method
CN103591780A (en) * 2013-01-04 2014-02-19 邹岳明 Main drying unit of slurry or powder continuous drying system
CN103913049A (en) * 2013-01-04 2014-07-09 邹岳明 Slurry or powder continuous drying system
WO2018179051A1 (en) * 2017-03-27 2018-10-04 株式会社加来野製作所 Pyrolysis device
KR20210096776A (en) * 2020-01-29 2021-08-06 성안이엔티주식회사 Vertical Hot Air Silo Dryer

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100233231B1 (en) * 1997-07-25 1999-12-01 정학철 Process device for food garbage
JP2006166805A (en) * 2004-12-16 2006-06-29 Mayekawa Mfg Co Ltd Method and apparatus for freezing, cooling and heating granule or the like
WO2012011600A1 (en) * 2010-07-23 2012-01-26 北海道特殊飼料株式会社 Drying device and drying method
CN103591780A (en) * 2013-01-04 2014-02-19 邹岳明 Main drying unit of slurry or powder continuous drying system
CN103913049A (en) * 2013-01-04 2014-07-09 邹岳明 Slurry or powder continuous drying system
CN103591780B (en) * 2013-01-04 2015-11-18 邹岳明 The main drying of the continuous drying system of slurry or powder
CN103913049B (en) * 2013-01-04 2016-03-16 邹岳明 The continuous drying system of slurry or powder
WO2018179051A1 (en) * 2017-03-27 2018-10-04 株式会社加来野製作所 Pyrolysis device
KR20210096776A (en) * 2020-01-29 2021-08-06 성안이엔티주식회사 Vertical Hot Air Silo Dryer

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Publication number Publication date
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