JPH01187061A - Continuous cereal grain swelling machine - Google Patents

Continuous cereal grain swelling machine

Info

Publication number
JPH01187061A
JPH01187061A JP63011794A JP1179488A JPH01187061A JP H01187061 A JPH01187061 A JP H01187061A JP 63011794 A JP63011794 A JP 63011794A JP 1179488 A JP1179488 A JP 1179488A JP H01187061 A JPH01187061 A JP H01187061A
Authority
JP
Japan
Prior art keywords
trough
grains
conveyer
granules
grain
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
JP63011794A
Other languages
Japanese (ja)
Other versions
JPH0650972B2 (en
Inventor
Kiyoshi Sekine
関根 清
Sunao Tsukada
直 塚田
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.)
Kikkoman Corp
Original Assignee
Kikkoman Corp
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 Kikkoman Corp filed Critical Kikkoman Corp
Priority to JP63011794A priority Critical patent/JPH0650972B2/en
Publication of JPH01187061A publication Critical patent/JPH01187061A/en
Publication of JPH0650972B2 publication Critical patent/JPH0650972B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To continuously and efficiently obtain swollen cereal grain fluid of good quality in a short time without compression breakage of the grains, by constituting the blades of screw conveyers for transferring the cereal grains in a grain-swelling machine for beans or cereals. CONSTITUTION:Grains of, e.g., beans or cereal are charged from the feeder 8 and sent through the first trough 2 by the first screw conveyer 5, then transferred by the first transfer means 9 to the second trough 3, then transferred to the third trough 4 in the same manner. At the same time, the solution is fed through pipes 12, 13 to swell the grains, the solution is drained from the drain outlet 14, when needed. In the meantime, the swollen grains were transferred through the third grain transfer 11 to the grain cutting-out mechanism 17. The blades W of the first through third screw conveyers 5-7 are made of porous plates W1 having such pores as the solution can pass through, but the grains cannot. The blade pitch in the first conveyer 5 is set gradually large toward the moving direction until the maximum at the midway of the conveyer, and kept constant since then. The blade pitch of the second conveyer 6 is made gradually larger in the conveying direction until at the midway, then kept at the maximum, and the third conveyer is kept constant at the maximum of the second conveyer 6.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、豆類、穀類の浸漬・膨潤装置に関する。[Detailed description of the invention] (Industrial application field) The present invention relates to a device for soaking and swelling beans and grains.

(従来の技術) 大豆、小豆などの豆類及び米、麦など穀類を加工する工
程には、水など液体に豆・穀類(以下粒体と記す)を浸
漬し、この液体にてふやけさせ次の磨砕、破砕にそなえ
る膨潤工程がある。
(Prior art) In the process of processing legumes such as soybeans and adzuki beans, and grains such as rice and wheat, beans and grains (hereinafter referred to as granules) are immersed in a liquid such as water, soaked in this liquid, and then processed into the next process. There is a swelling process in preparation for grinding and crushing.

豆腐製造工程における大豆の膨潤装置を例に以下に説明
する。
The soybean swelling device used in the tofu manufacturing process will be described below as an example.

従来、豆腐用大豆は良く水洗いし、容器に移し、水に漬
けて長時間放置する。浸漬水の温度を上げたとしても上
記浸漬時間は4〜5時間を要し、増産を図り難い。
Conventionally, soybeans for tofu are thoroughly washed with water, transferred to a container, soaked in water, and left for a long time. Even if the temperature of the immersion water is raised, the above immersion time takes 4 to 5 hours, making it difficult to increase production.

これの改良技術として、例えば特開昭62−26295
9号公報に示す装置が提案されている。この改良技術は
、予め脱皮し分割した大豆片を水または温水を張ったト
ラフに投入し、スクリューフィーダにて移動させる処理
技術である。
As an improved technique for this, for example, Japanese Patent Application Laid-Open No. 62-26295
A device shown in Publication No. 9 has been proposed. This improved technology is a processing technology in which soybean pieces that have been previously dehulled and divided are placed in a trough filled with water or warm water, and then moved using a screw feeder.

(発明が解決しようとする課題) しかしながら上記したスクリューフィーダで移動する処
理設備であっても、非脱皮、非分割の大豆に対しては膨
潤時間の短縮効果は小さい。
(Problems to be Solved by the Invention) However, even with the processing equipment that is moved by the above-mentioned screw feeder, the effect of shortening the swelling time on unhulled and undivided soybeans is small.

従って、表皮の有無にかかわらず効率良く処理できる装
置が切望されている。
Therefore, there is a strong need for a device that can efficiently treat the skin regardless of the presence or absence of the epidermis.

(課題を解決するための手段) このような要望に応えるべく、本発明は粒体を水平移送
するスクリューコンベアを備え、このスクリューコンベ
アの羽根を、粒体は通さずに液体を通す多孔板で形成す
る。
(Means for Solving the Problems) In order to meet such demands, the present invention includes a screw conveyor that horizontally transports granules, and the blades of this screw conveyor are made of perforated plates that allow liquid to pass through, but not granules. Form.

(作 用) 液体はコンベアの軸方向に流れて粒体に接触し、膨潤作
用を促進する。
(Function) The liquid flows in the axial direction of the conveyor and comes into contact with the particles, promoting the swelling effect.

(実施例) 以下に本発明の実施例を添付図面に基づいて説明する。(Example) Embodiments of the present invention will be described below based on the accompanying drawings.

第1図は本発明に係る連続膨潤装置平面図、第2図は本
発明に係るスクリューコンベアの羽根の拡大図、第3図
は第1図のA−A矢視図、第4図は同C−C矢視図、第
5図は同C−C矢視図である。
FIG. 1 is a plan view of a continuous swelling device according to the present invention, FIG. 2 is an enlarged view of the blades of a screw conveyor according to the present invention, FIG. 3 is a view taken along arrow A-A in FIG. 1, and FIG. A view taken along the line C-C, and FIG. 5 is a view taken along the line C-C.

連続膨潤装置1は、断面U字形の第1トラフ2の横に第
2トラフ3を、更に第1トラフの延長上に第3トラフ4
を第1図の如く配設し、これら第1・第2・第3トラフ
2,3.4には夫々第1・第2・第3スクリューコンベ
ア5,6.7を介設し、且つ第1トラフ2の図示右端上
方には粒体Bを投下する粒体供給機構8を臨ませ、第1
トラフ2出口と第2トラフ3人口との間には第1の粒体
移載機構9を設け、第2トラフ3出口と第3トラフ4人
口との間には第2の粒体移載機構1oを設け、第3トラ
フ4出口部分には第3の粒体移載機構11を設けて成る
The continuous swelling device 1 includes a second trough 3 beside a first trough 2 having a U-shaped cross section, and a third trough 4 on an extension of the first trough.
are arranged as shown in FIG. A granule supply mechanism 8 for dropping the granules B faces above the right end of the first trough 2 as shown in the figure.
A first granule transfer mechanism 9 is provided between the trough 2 outlet and the second trough 3 population, and a second granule transfer mechanism is provided between the second trough 3 outlet and the third trough 4 population. 1o, and a third granule transfer mechanism 11 is provided at the outlet of the third trough 4.

第1トラフ2の入口付近と第3トラフの出口付近には液
体を落下せしめる給液管12.13を臨ませ、第2トラ
フ3の隅(第1図の左上方向)には排液口14を付設し
である。
Near the inlet of the first trough 2 and near the outlet of the third trough, a liquid supply pipe 12.13 for dropping the liquid faces, and a drain port 14 is located at the corner of the second trough 3 (upper left direction in Fig. 1). It is attached.

第1スクリユーコンベア5の軸5aは第3スクリユーコ
ンベア7の軸をも兼ねる。この軸5aは第1トラフ2と
第3トラフ4とを貫通し、両端を水密シールを備えた軸
受2a、4aにて支承され、且つ一端は減速機付き電動
機の如き回転装置15に軸結合している。
The shaft 5a of the first screw conveyor 5 also serves as the shaft of the third screw conveyor 7. This shaft 5a passes through the first trough 2 and the third trough 4, is supported at both ends by bearings 2a and 4a provided with watertight seals, and is axially coupled to a rotating device 15 such as an electric motor with a reduction gear at one end. ing.

第2スクリユーコンベア6の軸6aは、前記軸5aと平
行に水密性軸受3a、3aに支承され、チェーン15a
1スプロケツト15bを介して、軸5aと同一方向に同
一速度で回転するように連結されている。
A shaft 6a of the second screw conveyor 6 is supported by watertight bearings 3a, 3a parallel to the shaft 5a, and a chain 15a.
1 sprocket 15b so as to rotate in the same direction and at the same speed as the shaft 5a.

前記軸5a、6aには、第2図に示す如き、羽根Wを螺
旋状に巻きつけ固定しである。
As shown in FIG. 2, blades W are spirally wound and fixed around the shafts 5a and 6a.

第1スクリユーコンベア5の羽根Wのピッチは、粒体B
の移動方向に徐々に大きくし、第2スクリユーコンベア
6の羽根Wのピッチは、途中まで徐々に大きくし、それ
以降は最大値に合せて一定とし、第3スクリユーコンベ
アフの羽根Wのピッチは、第2スクリユーコンベア6の
最大値に合せて一定としている。
The pitch of the blades W of the first screw conveyor 5 is
The pitch of the blades W of the second screw conveyor 6 is gradually increased in the moving direction of The pitch is kept constant according to the maximum value of the second screw conveyor 6.

第1・第2・第3スクリユーコンベアの羽根Wは、薄板
に通液の為の小孔りを多数穿設した多孔板W1で形成す
る。
The blades W of the first, second, and third screw conveyors are formed of a perforated plate W1 in which a large number of small holes for liquid passage are bored in a thin plate.

上記小孔りの径は、対象粒体Bが通り抜けない寸法に決
める。例えば、7〜12++uaの大豆に対しては小孔
りの径は4〜5■■とする。
The diameter of the small hole is determined so that the target particles B cannot pass through it. For example, for soybeans of 7 to 12++ ua, the diameter of the pores should be 4 to 5 ■■.

多孔板W1の開孔率は(単位面積当りの小孔りの面積和
)÷(単位面積)で表される。
The porosity of the perforated plate W1 is expressed as (sum of area of small holes per unit area)/(unit area).

本装置の開孔率は0.1〜0.5の範囲から選ぶものと
し、吸液性の良い粒体には小さく、悪い粒体には大きく
している。
The aperture ratio of this device is selected from the range of 0.1 to 0.5, and is set small for particles with good liquid absorption and large for particles with poor liquid absorption.

本実施例は、図示するように、二条のスクリューコンベ
ア軸5a、6aを平行に配置し、粒体Bを長方形の辺を
一巡させるようにして、装置長さを半減し、粒体供給機
構8と粒体切出し機構17とを装置略中央に並設できる
ようにしたことを特徴の一つとしている。
In this embodiment, as shown in the figure, the two screw conveyor shafts 5a and 6a are arranged in parallel, and the granules B are made to go around the sides of the rectangle, reducing the length of the device by half, and the granules supplying mechanism 8 One of the features is that the granule cutting mechanism 17 and the granule cutting mechanism 17 can be arranged side by side substantially in the center of the device.

その為に、第1・第2・第3トラフ2,3.4を順に連
絡する第1・第2の粒体移載機構9゜10を備えている
。以下にこれらの構成を詳述する。
For this purpose, first and second granule transfer mechanisms 9 and 10 are provided which sequentially connect the first, second and third troughs 2, 3.4. These configurations will be explained in detail below.

第3図は第1図のA−A矢視図であり、第1スクリユー
コンベアの軸5aには、スプーンの背のように湾曲させ
た掻き揚げ板9aを軸5aに平行にして固着し、この掻
き揚げ板9aの両端には、回転前方へ側板9b、9bを
立設している。また、これら側板9b、9b間に嵌り込
んで、掻き揚げ板9aに摺接するフラッパ9Cを第2ト
ラフ3の係止部3bにピン係止し揺動自在としている。
FIG. 3 is a view along arrow A-A in FIG. 1, and a scraping plate 9a curved like the back of a spoon is fixed to the shaft 5a of the first screw conveyor in parallel to the shaft 5a. At both ends of this scraping plate 9a, side plates 9b, 9b are erected in the rotationally forward direction. Further, a flapper 9C that fits between the side plates 9b and 9b and slides in contact with the scraping plate 9a is pin-locked to the locking portion 3b of the second trough 3 so as to be able to swing freely.

このように、第1の粒体移載機構9は、前記掻き揚げ板
9aと側板9b、9bとフラッパ9Cとから構成される
In this way, the first granule transfer mechanism 9 is composed of the scraping plate 9a, the side plates 9b, 9b, and the flapper 9C.

第4図は第1図のB−B矢視図であり、第2スクリユー
コンベアの軸6aに、掻き揚げ板10aを固設し、この
掻き揚げ板10a4−側板10b。
FIG. 4 is a view along the line B-B in FIG. 1, in which a scraping plate 10a is fixedly installed on the shaft 6a of the second screw conveyor, and the scraping plate 10a4-side plate 10b.

10bを立設した、第3図と同様の掻き揚げ板である。This is a scraping board similar to that shown in FIG.

この掻き揚げ板10aに摺接するフラッパ10cは図示
する如く湾曲し、第2トラフ3の係止部3Cに揺動自在
にピン係止されている。
The flapper 10c that comes into sliding contact with the scraping plate 10a is curved as shown in the figure, and is pin-locked to the locking portion 3C of the second trough 3 so as to be swingable.

このように、第2の粒体移載機構10は掻き揚げ板10
aと側板10b、10bとフラッパ10cとから構成さ
れる。
In this way, the second granule transfer mechanism 10 uses the scraping plate 10
a, side plates 10b, 10b, and a flapper 10c.

第1図のC−C矢視図である第5図は、第3の粒体移載
機構11を示し、この機構11は、第2の粒体移載機構
10と同様の掻き揚げ板11aと側板flb、llbと
フラッパllcとからなる。
FIG. 5, which is a view taken along the line C-C in FIG. It consists of side plates flb, llb and flapper llc.

第3の粒体移載機構11には、粒体切出し機構17が接
続している。
A grain cutting mechanism 17 is connected to the third grain transfer mechanism 11 .

第6図にて粒体切出し機構1フを説明すると、17aは
液体を張っであるホッパであり、このホッパ1フaの一
壁は前記第3の粒体移載機構11からの粒体Bを受けと
る受は斜面17bとし、ホッパ17aの下端にはロータ
リ弁17cを配置し、このロータリ弁1フCの下方に傾
斜した網板17dと、排水樋17eを配置する。
To explain the granule cutting mechanism 1F in FIG. The receiver for receiving water is a slope 17b, a rotary valve 17c is arranged at the lower end of the hopper 17a, a mesh plate 17d inclined downwardly of the rotary valve 1C, and a drainage gutter 17e are arranged.

図中17fは前記網板17dを囲んで垂下する下部シュ
ートであり、17gは網板17d上を摺動する押しバー
である。押しバー17gはシリンダユニット17hの作
用にて進退する。
In the figure, 17f is a lower chute that hangs down surrounding the mesh plate 17d, and 17g is a push bar that slides on the mesh plate 17d. The push bar 17g moves forward and backward under the action of the cylinder unit 17h.

以上の構成からなる連続膨潤装置の作用を以下に説明す
る。
The operation of the continuous swelling device having the above configuration will be explained below.

第1図の粒体供給機構8から落下投入された粒体Bは、
第1トラフ2の中を第1スクリユーコンベア5の作用に
て連続的に進行し、第1の粒体移載機構9に至る。
The granules B dropped from the granule supply mechanism 8 in FIG.
The particles continuously advance through the first trough 2 under the action of the first screw conveyor 5 and reach the first granule transfer mechanism 9 .

第1の粒体移載機構9で(第3図参照)、粒体Bは掻き
揚げ板9aに載り、徐々に上昇する。フラッパ9Cが掻
き揚げ板9aの根元から先端に向って摺接、移動しつつ
、粒体Bをすくい揚げ、結果図示りに示す如く、フラッ
パ9Cの斜面に沿つて粒体Bは第2トラフ3へ落下する
。この際、側板9b、9bは粒体Bが軸5a方向にこぼ
れるのを防止する。また、フラッパ9CはD位装置を上
限とするので第2トラフ3側へ倒れ込むことは無い。
In the first granule transfer mechanism 9 (see FIG. 3), the granules B are placed on a scraping plate 9a and gradually ascend. The flapper 9C slides into contact with and moves from the base of the scraping plate 9a toward the tip, scooping up the grains B, and as a result, as shown in the figure, the grains B move along the slope of the flapper 9C into the second trough 3. fall to At this time, the side plates 9b prevent the grains B from spilling in the direction of the axis 5a. Furthermore, since the upper limit of the flapper 9C is at the D position device, it will not fall down toward the second trough 3 side.

このようにして第2トラフ3へ穆った粒体Bは第2スク
リユーコンベア6の作用にて(第1図右方へ)前進し、
第2の粒体移載機構10で第3トラフ4へ移載され、第
3トラフ4内を第3スクリユーコンベア7の作用にて(
第1図左方へ)前進する。
The grains B thus sieved to the second trough 3 are moved forward (toward the right in FIG. 1) by the action of the second screw conveyor 6.
The particles are transferred to the third trough 4 by the second granule transfer mechanism 10, and moved inside the third trough 4 by the action of the third screw conveyor 7 (
Move forward (toward the left in Figure 1).

一方、本装置1は、粒体Bの投入、抽出部分に夫々設け
た給液管12.13から常時定量の液体を供給している
。給液管12からの液体は第1トラフ2内を粒体Bを包
みつつ、羽根Wの小孔h・・・を通って、軸5aと略平
行に前進し、第1の粒体移載機構9部分から第2トラフ
3へ移り、排液口14に至る。
On the other hand, this device 1 constantly supplies a fixed amount of liquid from liquid supply pipes 12 and 13 provided at the input and extraction portions of the granules B, respectively. The liquid from the liquid supply pipe 12 wraps the particles B in the first trough 2, passes through the small holes h of the vanes W, advances approximately parallel to the axis 5a, and transfers the particles to the first trough 2. It moves from the mechanism 9 portion to the second trough 3 and reaches the drain port 14.

また、給液管13からの液体は、第3トラフ4−第2の
粒体移載機構1〇−第2トラフ3の順路で、粒体Bに対
向して流れつつ排液口14に至る。
In addition, the liquid from the liquid supply pipe 13 flows in the order of the third trough 4 - the second granule transfer mechanism 10 - the second trough 3 and reaches the liquid drain port 14 while flowing against the granules B. .

即ち、本実施例では、膨潤工程を前期、後期に部分し、
前期を第1トラフ2で、後期を第2・第3トラフ3.4
で行わせている。
That is, in this example, the swelling process is divided into the first half and the second half,
First trough 2 in the first half, second and third trough 3.4 in the second half
I'm having it done.

前期では、粒体Bの膨潤が盛んであると同時に、抽出物
の抽出が盛んであり、これらを速やかに除き、また後期
では粒体Bの浄化を要す。
In the early stage, the swelling of the granules B is active, and at the same time, the extraction of extracts is also active, and these must be removed promptly, and the granules B must be purified in the latter stage.

よって、前期の平行流れで膨潤を促進し、後期の対向流
れで粒体Bは前進する程抽出物の少ない液体に接し浄化
する。
Therefore, the parallel flow in the early stage promotes swelling, and the counter flow in the latter stage allows the granules B to come into contact with a liquid containing less extractables and be purified as they move forward.

尚、工程の途中まではスクリューコンベアの羽根Wのピ
ッチが徐々に大きくなるので、粒体Bの占有空間が拡大
し、粒体B相互の押圧力の増加を防ぐので、粒体Bの圧
縮破壊は免れる。
In addition, the pitch of the blades W of the screw conveyor gradually increases until the middle of the process, so the space occupied by the granules B expands, and this prevents an increase in the pressing force between the granules B, thereby preventing compressive fracture of the granules B. is spared.

このようにして膨潤工程を終えた粒体Bは、第3の粒体
移載機構11の作用にて、第3トラフ11から粒体切出
し機構17に移される。粒体Bはホッパの斜面17bを
滑り落ちるが、間欠的に回動するロータリ弁17cがそ
の空室に空気を閉じ込め、この空気をホッパ17aに臨
んだ際に放出し、この空気気泡がホッパ1フa内を攪拌
するので上記粒体Bは適当に分散される。
The granules B that have completed the swelling step in this manner are transferred from the third trough 11 to the granule cutting mechanism 17 by the action of the third granule transfer mechanism 11 . The granules B slide down the slope 17b of the hopper, but the rotary valve 17c, which rotates intermittently, traps air in its empty chamber and releases this air when it faces the hopper 17a, causing these air bubbles to flow into the hopper 1st floor. Since the inside of a is stirred, the particles B are appropriately dispersed.

ロータリ弁17cから水とともに落下する粒体Bは網板
17dに載り、水のみが下の排水樋17eへ落下する。
The particles B falling together with water from the rotary valve 17c are placed on the net plate 17d, and only the water falls into the drainage gutter 17e below.

シリンダユニット17hを作動し、押しバー17gにて
網板17d上の粒体Bを下部シュート17fへ落下せし
める。
The cylinder unit 17h is operated and the push bar 17g causes the particles B on the mesh plate 17d to fall into the lower chute 17f.

尚、本実施例ではスクリューコンベアを二条三本で、構
成したが、これに限るものではなく、−条のみ若しくは
三条以上で装置を形成してもよい。
In this embodiment, the screw conveyor is constructed with two or three threads, but the invention is not limited to this, and the device may be formed with only one thread or three or more threads.

(発明の効果) 以上に説明した如く、本発明によれば、スクリューコン
ベアにて連続して膨潤(6埋ができ、コンベア軸方向の
液体流れによって膨潤作用時間を短縮し、コンベアの羽
根ピッチを徐々に大きくして粒体の圧縮破壊を防ぐので
、高品質の膨潤粒体を効率よく連続して生産可能である
(Effects of the Invention) As explained above, according to the present invention, the screw conveyor allows for continuous swelling (swelling), and the liquid flow in the axial direction of the conveyor shortens the swelling action time, and the pitch of the blades of the conveyor can be reduced. Since the granules are gradually enlarged to prevent compressive destruction of the granules, it is possible to efficiently and continuously produce high-quality swollen granules.

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

第1図は本発明に係る連続膨潤装置平面図、第2図は本
発明に係るスクリューコンベアの羽根の拡大図、第3図
は第1図のA−A矢視図、第4図は同C−C矢視図、第
5図は同C−C矢視図、第6図は粒体切出し機構の断面
図である。 尚、図面中、1は連続膨潤装置、5,6.7は第1.第
2.第3スクリユーコンベア、Bは粒体、Wはスクリュ
ーコンベアの羽根、Wlは多孔板である。
FIG. 1 is a plan view of a continuous swelling device according to the present invention, FIG. 2 is an enlarged view of the blades of a screw conveyor according to the present invention, FIG. 3 is a view taken along arrow A-A in FIG. 1, and FIG. FIG. 5 is a view taken along the line C--C, and FIG. 6 is a cross-sectional view of the granule cutting mechanism. In addition, in the drawing, 1 is a continuous swelling device, 5, 6.7 is a first. Second. In the third screw conveyor, B is a granule, W is a screw conveyor blade, and Wl is a perforated plate.

Claims (1)

【特許請求の範囲】[Claims] 豆類などの粒体を液体に浸漬して膨潤させる膨潤装置に
おいて、前記膨潤装置には、前記粒体を水平移送するス
クリューコンベアを備え、このスクリューコンベアの羽
根は、前記液体を通過せしめ、粒体を非通過とする多孔
板で形成したことを特徴とする連続膨潤装置。
In a swelling device that swells granules such as beans by immersing them in a liquid, the swelling device includes a screw conveyor that horizontally transports the granules, and the blades of this screw conveyor allow the liquid to pass through and swell the granules. A continuous swelling device characterized in that it is formed of a perforated plate that does not allow water to pass through.
JP63011794A 1988-01-21 1988-01-21 Continuous swelling device Expired - Fee Related JPH0650972B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63011794A JPH0650972B2 (en) 1988-01-21 1988-01-21 Continuous swelling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63011794A JPH0650972B2 (en) 1988-01-21 1988-01-21 Continuous swelling device

Publications (2)

Publication Number Publication Date
JPH01187061A true JPH01187061A (en) 1989-07-26
JPH0650972B2 JPH0650972B2 (en) 1994-07-06

Family

ID=11787813

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63011794A Expired - Fee Related JPH0650972B2 (en) 1988-01-21 1988-01-21 Continuous swelling device

Country Status (1)

Country Link
JP (1) JPH0650972B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62262959A (en) * 1986-05-09 1987-11-16 Asahi Kogyo Kk Processing of soybean and continuous processing apparatus

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62262959A (en) * 1986-05-09 1987-11-16 Asahi Kogyo Kk Processing of soybean and continuous processing apparatus

Also Published As

Publication number Publication date
JPH0650972B2 (en) 1994-07-06

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