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JPS5925592B2 - Konjac manufacturing equipment - Google Patents
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JPS5925592B2 - Konjac manufacturing equipment - Google Patents

Konjac manufacturing equipment

Info

Publication number
JPS5925592B2
JPS5925592B2 JP55013392A JP1339280A JPS5925592B2 JP S5925592 B2 JPS5925592 B2 JP S5925592B2 JP 55013392 A JP55013392 A JP 55013392A JP 1339280 A JP1339280 A JP 1339280A JP S5925592 B2 JPS5925592 B2 JP S5925592B2
Authority
JP
Japan
Prior art keywords
tank
raw material
blade
pipe
pump
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
Application number
JP55013392A
Other languages
Japanese (ja)
Other versions
JPS56109566A (en
Inventor
彦美 舘岡
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP55013392A priority Critical patent/JPS5925592B2/en
Publication of JPS56109566A publication Critical patent/JPS56109566A/en
Publication of JPS5925592B2 publication Critical patent/JPS5925592B2/en
Expired legal-status Critical Current

Links

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  • Preparation Of Fruits And Vegetables (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Description

【発明の詳細な説明】 本発明は、コンニヤクの製造装置に関する。[Detailed description of the invention] The present invention relates to a konjac manufacturing apparatus.

従来この種コンニヤクの製造装置としては、例えば特公
昭45−39029、特公昭49一39832公報など
によつて開示されているように、コンニヤク原料を練合
して最もよい条件の生のり状態とする工程装置と、凝固
剤である石灰水を混和させる工程装置とを各別に設ける
と共にこれらを結合したものによつて構成されており、
更にその手段としては原料の練合、生のりに凝固剤を加
える工程が全て密閉された状態で行われている。このよ
うに密閉された真空状態下で行われることから触気作用
が殆んどなく、従つて呼吸作用があるとされているコン
ニヤク原料にとつて苛酷な条件下で処理せしめられるた
め、コンニヤクの生命である弾力性、コク、舌触わりな
ど全ての点において手作りのものより劣る欠点がみられ
る。
Conventionally, this kind of konjac manufacturing apparatus is disclosed in, for example, Japanese Patent Publication No. 45-39029, Japanese Patent Publication No. 49-39832, etc., which involves kneading konjac raw materials to obtain a raw paste state under the best conditions. It is constructed by separately providing process equipment and a process equipment for mixing lime water, which is a coagulant, and combining them.
Furthermore, the process of kneading the raw materials and adding a coagulant to the raw seaweed is all carried out in a sealed state. Because the process is carried out in a sealed vacuum, there is almost no tactile effect, and the raw material for konjac, which is said to have a respiratory effect, is processed under harsh conditions. It has the disadvantage of being inferior to handmade products in all aspects of life, such as elasticity, richness, and texture.

本発明は、このような実情に鑑みなされたもので、簡単
な構成と合理的手段によつて従来技術の問題点を解消せ
しめ、漏斗状槽内に配設せる枠伏翼と、これに自転公転
可能に設けたスクリュー翼とにより効率のよい撹拌練合
を行わせ、加えて開放型槽による原料の触気作用、及び
循環パイプによる触気循環作用とにより充分な原料の触
気を行わせ、手造りの最高品質と同等なコンニヤクが得
られる装置を提供せんとするものである。次に本発明の
実施例を図面について説明すると。
The present invention has been made in view of these circumstances, and solves the problems of the prior art with a simple configuration and rational means. Efficient stirring and kneading is carried out by the screw blades installed so that they can revolve, and in addition, sufficient aeration of the raw materials is carried out by the tactile action of the raw materials by the open tank and the tactile circulation action by the circulation pipe. We aim to provide a device that allows you to obtain konnyaku that is equivalent to the highest quality hand-made konnyaku. Next, embodiments of the present invention will be described with reference to the drawings.

1は上面を開放し下部を漏斗状に形成した円筒形状の槽
であつて、該槽1の内部軸心方向には上端に伝動部を有
し下端を槽底に接触しないよう近接させた回転軸2が出
入自在に装入してあり、またこの回転軸2のーー側には
上記槽1の垂直内壁面に近接する垂直翼3と、槽の傾斜
内壁面に近接する斜翼4と、上記垂直翼3の上端と回転
軸2とを結ぶ水平翼5とからなる枠状翼6が設けてある
Reference numeral 1 denotes a cylindrical tank with an open top and a funnel-shaped bottom.In the direction of the internal axis of the tank 1, there is a transmission section at the top end, and a rotating mechanism with the bottom end close to the bottom of the tank so as not to contact it. A shaft 2 is inserted into and out of the rotary shaft 2, and on the - side of the rotary shaft 2 are vertical blades 3 close to the vertical inner wall surface of the tank 1, and oblique blades 4 close to the inclined inner wall surface of the tank. A frame-shaped wing 6 is provided, which includes a horizontal wing 5 that connects the upper end of the vertical wing 3 and the rotating shaft 2.

この垂直翼3は第3図に示す如くこの垂直翼を構成する
板材が矢印で示す回転方向に対して翼の外側縁が後方と
なるように斜設即に槽壁面に対し後退角をもつて臨むよ
うにしてあり、原料を攪拌且つ練成する機能かもたせて
ある。また上記斜翼4も第4図に示すように後退角をも
たせ、垂直翼3と同様に原料を攪拌、練成する作用が与
えられているし,加えて原料を後述するポンプ方向に誘
導する作用も有している。
As shown in Fig. 3, this vertical blade 3 is installed obliquely so that the plate material constituting the vertical blade faces backward with respect to the direction of rotation shown by the arrow, and has a receding angle with respect to the tank wall surface. It is designed so that it can be viewed directly, and also has the function of stirring and kneading raw materials. The oblique blades 4 also have a swept angle as shown in Fig. 4, and have the function of stirring and kneading the raw materials in the same way as the vertical blades 3, and in addition, they also guide the raw materials in the direction of the pump, which will be described later. It also has an effect.

また上記水平翼5も第4図から明らかなように上記各翼
3,4と同様に後退角を有しており,原料を攪拌練合す
る作用に加えて上層の原料を下方に誘導対流せしめる作
用をもつている。
Further, as is clear from Fig. 4, the horizontal blade 5 also has a receding angle like the blades 3 and 4, and in addition to stirring and kneading the raw materials, it also induces downward convection of the raw material in the upper layer. It has an effect.

7は上記枠状翼6を構成する水平翼5と斜翼4の中間部
間に垂直に而も回転自在に軸架せしめたスクリユ一翼で
あつて,該スクリユ一翼7は板材をひと捻りした程度の
ピツチの大きなものである。
Reference numeral 7 denotes a screw blade that is vertically and rotatably mounted between the intermediate portions of the horizontal blade 5 and oblique blade 4 that constitute the frame-shaped blade 6, and the screw blade 7 is approximately the same as a twisted plate material. It's a big one.

そしてこのスクリユ一翼7に設けた上方の軸8を上方に
延長し,この上端にピニオン9を設けると\もにこのピ
ニオン9を上記回転軸2にその中心部を遊嵌した径大の
ギヤ10に嵌合せしめ6このスクリユ一翼7に対し回転
軸2の回転による公転と,ギヤー10とピニオン9によ
る軸8の回転で自転運動を与えるようにし6更にスクリ
ユ一翼7の回転により原料を万偏なく攪拌,対流させる
。尚特に図示してないが6上記ギヤー10に代えてリン
グ状のインターナルギヤ一を用いても同様な作用が得ら
れるものであるため6実施例のものに特定されることは
ない。また上記槽1の下端部にはパイプ11を介してギ
ヤーポンプなどのポンプ12が接続してあり、該ポンプ
12の吐出端は槽内の約30%に相当する量の触気させ
なから絶えず槽1の上部に帰戻循環投入せしめるパイプ
13が接続されている。
If the upper shaft 8 provided on this screw blade 7 is extended upward and a pinion 9 is provided at its upper end, this pinion 9 will be connected to a gear 10 with a large diameter whose center part is loosely fitted to the rotating shaft 2. 6 This screw blade 7 is caused to revolve by the rotation of the rotary shaft 2 and rotate by the rotation of the shaft 8 by the gear 10 and pinion 9. Stir and convect. Although not particularly shown in the drawings, the same effect can be obtained even if a ring-shaped internal gear 1 is used in place of the gear 10 described above, so the invention is not limited to the sixth embodiment. Furthermore, a pump 12 such as a gear pump is connected to the lower end of the tank 1 via a pipe 11, and the discharge end of the pump 12 constantly pumps air into the tank, which corresponds to about 30% of the inside of the tank. A pipe 13 for supplying return circulation is connected to the upper part of the pipe 1.

このパイプ13の水平部に切換バルブ14を介して後述
する定量充填機のホッパ一に原料を供給するパイプ15
が接続してあり6またこの切換バルブ14と上記循環用
パイプ13の垂直部下端との間のパイプ部をU字状に屈
折せしめ6該屈折部最下端にバルブ16を備え且つ上記
ホツパ一にパイプ13内の原料を流下供給するパイプ1
7が設けてある。18は一般に使用されている定量充填
機であつて,該定量充填機は、ホツパ一196一方が原
料を定量吸引したときに他方か原料を吐出するようにし
た2本のシリンダー20,21及び該両シリンダー20
,21の両吐出側を連通させたノズルパイプ22などに
よつて構成されている。
A pipe 15 that supplies raw materials to a horizontal portion of this pipe 13 via a switching valve 14 to a hopper of a quantitative filling machine to be described later.
The pipe section between this switching valve 14 and the vertical lower end of the circulation pipe 13 is bent into a U-shape, and the valve 16 is provided at the lowest end of the bent section, and the pipe section is connected to the hopper. Pipe 1 that supplies the raw material in pipe 13 downstream
7 is provided. Reference numeral 18 denotes a generally used quantitative filling machine, which consists of two cylinders 20 and 21, each of which has a hopper 196, in which when one sucks a fixed amount of raw material, the other discharges the raw material. both cylinders 20
, 21, and a nozzle pipe 22 that communicates with both discharge sides.

図中23はコンニヤク整形包装用の角形容器24を移送
せしめるコンベヤーなどの移送体,25は容器内に充填
された盛り上り状の原料を押圧整形するための押圧体,
26は該押圧体25によつて原料との間に挟圧支持され
容器24と押圧体25の移動によつて一定の長さだけ引
き出されるコイル伏のフイルムで,該フイルムは蓋とし
て用いられる。
In the figure, 23 is a transporting body such as a conveyor for transporting a rectangular container 24 for shaping and packaging konjac, 25 is a pressing body for pressing and shaping the raised material filled in the container,
Reference numeral 26 denotes a coiled film which is supported by the pressing body 25 and the raw material and is pulled out by a certain length by the movement of the container 24 and the pressing body 25, and is used as a lid.

また27は押圧体25と一緒に移動し上下動しながらフ
イルム26を上記容器24の周縁フランジに一体融着し
且つヒートカツトせしめるヒーターである。
A heater 27 moves together with the pressing body 25 and moves up and down to integrally fuse and heat-cut the film 26 to the peripheral flange of the container 24.

ヒートカツトの代りにカツタ一28の共同作用でフイル
ムを切断してもよい。そして上記押圧体25とヒーター
27は後述する作用説明のように.水平方向の往復運動
と上下動を父互連続的即ち矩形状の運動を行うようにし
てある。
The film may be cut by the joint action of the cutter 28 instead of the heat cut. The pressing body 25 and heater 27 function as described below. The reciprocating motion in the horizontal direction and the vertical motion are mutually continuous, that is, rectangular motion is performed.

尚この定量充填機及び包装機に続いてコンニヤク原料を
凝固させるためのポール装置が連続的に接続されるが,
この装置については適宜のものが使用しうるため省略し
てある。図中29は大中小の3つの脚30,31,32
を備えたセンサーで,原料が中間の脚31から離れたと
きに回路が閉じポンプ12が駆動して原料をホツパ一1
9に供給し.供給原料レベルが最短の脚32に接したと
きにポンプ12の駆動が停止するようにしたもので,ホ
ツパ一内に常に所要量の原料が供給蓄溜されるようにし
てある。
A pole device for coagulating the konjac raw material is continuously connected to this quantitative filling machine and packaging machine.
This device is omitted because any suitable device can be used. 29 in the figure is three large, medium and small legs 30, 31, 32
When the raw material leaves the intermediate leg 31, the circuit closes and the pump 12 is activated to move the raw material to the hopper.
Supply to 9. The drive of the pump 12 is stopped when the feed material level touches the shortest leg 32, so that the required amount of material is always supplied and stored in the hopper.

次にこの装置を用いたコンニヤクの製造方法について実
施例を説明すると次の通りである。
Next, an example of a method for producing konjac using this apparatus will be described as follows.

パイプ13の水平部に設けた切替バルブ14を操作して
該パイプ13の定量充填機への連通を遮断した伏態にし
ておく。この状態で槽1内に所定量の水(20〜25℃
)を容れ回転軸2及びポンプ12を比較的低速に回転駆
動させる。
A switching valve 14 provided on the horizontal portion of the pipe 13 is operated to place the pipe 13 in a down position, cutting off communication with the quantitative filling machine. In this state, a predetermined amount of water (20~25℃) is placed in tank 1.
), and the rotating shaft 2 and pump 12 are driven to rotate at a relatively low speed.

従つて槽内の水は回転軸2に設けた枠状翼6とスクリユ
一翼7とによつて攪拌され且つポンプ12の作用でパイ
プ13を通つて絶えず循環される。次いで、この槽1内
に所定量6即ち水量の約35〜37分の1に相当するコ
ンニヤク原料(マンナン粉)を投入し更に攪拌練合を続
けると,コンニヤク原料は徐々に膨潤溶融(ゲル化)し
6更に枠状翼6.スクリユ一翼7の攪線練合作用と原料
の触気作用6加えて,パイプ13による循壊触気作用と
によつて,約15〜30分後には最もよい生のり条件(
粘り,光沢など)となる。
Therefore, the water in the tank is agitated by the frame-shaped blades 6 and the screw blades 7 provided on the rotary shaft 2, and constantly circulated through the pipe 13 by the action of the pump 12. Next, a predetermined amount 6 of konjac raw material (mannan powder) corresponding to about 1/35 to 37 of the amount of water is put into this tank 1, and stirring and kneading are continued. As a result, the konjac raw material gradually swells and melts (gels). ) and 6 further frame-shaped wings 6. Due to the stirring wire kneading action of the screw blade 7, the tactile action of the raw materials 6, and the circulating tactile action of the pipe 13, after about 15 to 30 minutes, the best green glue condition (
(stickiness, gloss, etc.).

このように原料が最もよい生のり条件となつた時に回転
軸2の回転数を急激に高め6この状態で約1070fM
度の適量の石灰水(凝固液)を単に投入するか或は枠伏
翼とスクリユ一翼による攪拌練合部に追従させながら投
入してこれを生のりに均等に且つ素早く混合すると約1
分未満の短かい時間のうちに生のりはピック色になる。
In this way, when the raw material reaches the best raw glue condition, the rotation speed of the rotating shaft 2 is rapidly increased to about 1070 fM in this state.
If you simply add an appropriate amount of lime water (coagulating liquid) or let it follow the stirring and kneading section made of frame folding blades and screw blades and mix it evenly and quickly with the raw seaweed, it will produce approximately 1.
In less than a minute, the raw seaweed becomes pickled color.

この時点で回転軸2の回転を停止すると共に切換バルブ
14を定量充填機側に切換え、またバルブ16を開くこ
とによつて槽1内の原料はポンプ12の作用で定量充填
機18のホツパ一19内に供給され、また一方循環用パ
イプ13内に残溜せる原料は自重流下してホツパ一19
内に供給せしめられる。
At this point, the rotation of the rotating shaft 2 is stopped, the switching valve 14 is switched to the quantitative filling machine side, and the valve 16 is opened. The raw material that is supplied into the hopper 19 and remains in the circulation pipe 13 flows down under its own weight to the hopper 19.
be supplied internally.

ホツパ一19内に所要量の原料が供給されると2本平行
したシリンダー20,21が上述のように交互に働き常
に定量の原料がノズルパイプ22から吐出せしめられ、
移送体23上の容器24内に定量充填される。
When the required amount of raw material is supplied into the hopper 19, the two parallel cylinders 20 and 21 work alternately as described above, so that a constant amount of raw material is always discharged from the nozzle pipe 22.
A fixed amount is filled into the container 24 on the transfer body 23.

容器24の中に原料が盛り上り状に充填された容器24
は移送体23の移動によつて一定の距離だけ移送される
とこの位置で押圧体25が下降しフイルム26を介し盛
り上り状の原料を圧潰的に押圧整形して容器24内にム
ラなく充填せしめる。
A container 24 filled with raw materials in a mounded shape
When the material is transferred a certain distance by the movement of the transfer body 23, the press body 25 descends at this position, crushingly presses and shapes the bulge-shaped raw material through the film 26, and fills the container 24 evenly. urge

そしてフイルム26を挟んだ状態で容器24は移送体2
3の運動によつて更に一定距離だけ移動する。このとき
上記押圧体25もそのま\の状態で追従移動せしめられ
,次いでこの押圧体25の外周に設けたヒーター27が
下降してフイルム26と容器24のフランジ部とをヒー
トシールすると共にフイルムをカツタ一28によりカツ
トしカツタ一は上昇退避する。
Then, the container 24 is transferred to the transfer body 2 with the film 26 sandwiched therebetween.
By the movement in step 3, it moves further by a certain distance. At this time, the pressing body 25 is also moved in the same state, and then the heater 27 provided on the outer periphery of the pressing body 25 is lowered to heat-seal the film 26 and the flange of the container 24, and also seal the film. The cutter 28 cuts, and the cutter 1 moves upward and retreats.

内カツタ一を用いずにヒートカツトすることも可能であ
る。この作業が済むと押圧体25とヒーター27が上昇
し更に移送体23の進行方向と逆方向に移動して再び上
記と同様な作用を繰り返し行う。
It is also possible to heat cut without using the inner cutter. When this operation is completed, the pressing body 25 and the heater 27 are raised and further moved in the direction opposite to the traveling direction of the transfer body 23, and the same operation as described above is repeated again.

またフイルムによる施蓋が完了した容器は任意のポール
装置に送られて加熱処理され原料は凝固しコンニヤクと
なる。また原料または粘性液を連続的に充填包装する場
合には6第5図に示すように槽1a,1b,1cを複数
個並設しておき、各槽における原料または粘性液の製造
時間を段階的にずらしておくことにより槽1aで作られ
た原料または粘性液を供給充填後バルブ14によつて槽
1bに切り換え、槽1bが充填に連つているときに槽1
a内で上述の原料または粘性液製造を行い、槽1b内の
原料または粘性液充填が終つた時点で槽1cに切換える
ようになし、原料または粘性液が絶えず定量充填機18
に供給されるようにしたものである。
Furthermore, the container that has been covered with a film is sent to an arbitrary pole device and is heat-treated to solidify the raw material and turn it into konnyaku. In addition, when continuously filling and packaging raw materials or viscous liquids, multiple tanks 1a, 1b, and 1c are arranged in parallel as shown in Figure 5, and the production time of raw materials or viscous liquids in each tank is staged. After supplying and filling the raw material or viscous liquid made in tank 1a, the valve 14 switches to tank 1b, and when tank 1b is in the process of filling, tank 1
The above-mentioned raw material or viscous liquid is produced in tank 1b, and when the filling of the raw material or viscous liquid in tank 1b is completed, it is switched to tank 1c, so that the raw material or viscous liquid is constantly supplied to quantitative filling machine 18.
It was designed to be supplied to

尚回転軸2の駆動停止6切換バルブ146バルブ16の
開閉切換などは制御装置により自動的に行わせるように
することが望ましく,これらは全て幾多実験の結果から
プログラムされるものである。また上記実施例とは全く
異つた製造方法も可能であり.その手段について説明す
ると次の通りである。
It is preferable that the control device automatically performs such operations as stopping the drive of the rotary shaft 2 and opening/closing the switching valve 146 and the valve 16, and these are all programmed based on the results of numerous experiments. Furthermore, a manufacturing method completely different from the above example is also possible. The means for doing so will be explained as follows.

パイプ13の水平部に設けた切替バルブ14を操作して
該パイプ13の定量充填機への連通を遮断した伏態にし
ておく。
A switching valve 14 provided on the horizontal portion of the pipe 13 is operated to place the pipe 13 in a down position, cutting off communication with the quantitative filling machine.

この状態で槽1内に所定量の水(20〜25℃)を次い
で凝固に必要な所要量の石灰水(約1070濃度)を予
め容れておき,槽1内の液を枠状翼6とスクリユ一翼7
とによつて攪拌練合しつ\この中に所要量(水の約30
分の1量)のコンニヤク原料を容れる。
In this state, a predetermined amount of water (20 to 25°C) and then a required amount of lime water (approximately 1070 concentration) necessary for coagulation are placed in the tank 1, and the liquid in the tank 1 is mixed with the frame-shaped blade 6. Sukuriyu Ichiyoku 7
Stir and knead. Add the required amount (approximately 30 ml of water) to this.
Add 1/2 of the amount of konjac ingredients.

このコンニヤク原料の量は上述した従来の製法に比べて
ゲル化量か少ないためにこの製造のものより多くの原料
を使用するものである。上記の状態で攪拌練合作用を約
3〜7分続けると原料粒子の一部が膨潤溶融(ゲル化)
し槽内液に粘りが生じ凝固が始まりかけた時点で上記回
転軸2の回転を止め枠伏翼6とスクリユ一翼7の攪拌練
合作用を停止せしめる。
Since the amount of konjac raw material is less than that of the conventional production method described above, more raw material is used than in this production. If the stirring and kneading action is continued for about 3 to 7 minutes in the above conditions, some of the raw material particles will swell and melt (gel).
When the liquid in the tank becomes sticky and begins to solidify, the rotation of the rotating shaft 2 is stopped and the stirring and kneading action of the frame flap blade 6 and the screw blade 7 is stopped.

そして切換バルブ14を定量充填機18側に切換え原料
粒子が残つた状態の粘性液をポンプ12の作用でホツパ
一19内に供給せしめる。
Then, the switching valve 14 is switched to the quantitative filling machine 18 side, and the viscous liquid with the raw material particles remaining is supplied into the hopper 19 by the action of the pump 12.

一方循環用パイプ13内に残存せる液はバルブ16を開
くことによりホツパ一19内に自重流下して供給される
。ホツパ一19内に所要量の粘性液が供給されると2本
平行したシリンダー20,21が上述のように交互に働
き常に定量の原料がノズルパイプ22から吐出せしめら
れ,移送体23上の容器24内に定量充填される。
On the other hand, by opening the valve 16, the liquid remaining in the circulation pipe 13 flows down by its own weight into the hopper 19 and is supplied. When the required amount of viscous liquid is supplied into the hopper 19, the two parallel cylinders 20 and 21 work alternately as described above to constantly discharge a fixed amount of raw material from the nozzle pipe 22, and the container on the transfer body 23. 24 is filled in a fixed quantity.

容器24の中に粘性液が充填された容器24は移送体2
3の運動によつて一定の距離だけ移送され,この位置で
押圧体25が下降しフイルム26を介して充填された粘
性液を押圧整形し6そしてフイルムを挟んだ状態で容器
24は移送体23の運動によつて更に一定距離だけ移動
する。
The container 24 filled with viscous liquid is the transporter 2
The container 24 is transferred a certain distance by the movement of 3, and at this position the pressing body 25 descends to press and shape the filled viscous liquid through the film 26.The container 24 is then moved to the conveying body 23 with the film sandwiched between them. It moves a certain distance further due to the movement of .

このとき上記押圧体25もそのま\の状態で追従移動せ
しめられ6次いでこの押圧体25の外周に設けたヒータ
ー27が下降してフイルム26と容器24のフランジ部
とをヒートシールすると共にフイルムをヒートカツトす
る。
At this time, the pressing body 25 is also moved in the same state, and then the heater 27 provided on the outer periphery of the pressing body 25 is lowered to heat-seal the film 26 and the flange of the container 24, and also seal the film. Heat cut.

この作業が適むと押圧体25とヒーター27が上昇し更
に移送体23の進行方向と逆方向に移動して再び上記と
同様な作用を繰り返し行う。
When this operation is completed, the pressing body 25 and the heater 27 are raised and further moved in the direction opposite to the advancing direction of the transporting body 23, and the same action as described above is repeated again.

またフイルムによる施蓋が完了した容器内の粘性液は石
灰である凝固剤が徐々に粒子中に入り込んではいるが,
この状態で加熱処理するため凝固が完了しマンナ粒子が
点在した伏態の製品が得られる。このように本発明によ
れば,同一槽内において,コンニヤク原料を攪拌練合す
ることにより6生のり化と石灰水の配合による凝固可能
な原料を生産することができ6特に.枠状翼6を構成す
る垂直翼6斜翼,水平翼に夫々後退角をもたせ、かつ、
枠状翼にスクリユ一翼を設けたことによつて原料の攪拌
.練成作用が有効に行われるとともに、原料の触気作用
が活発に行われ,更にポンプとパイプ13による原料の
循環触気作用力功めることによつて.更に原料の触気作
用が増大されることから、得られるコンニヤクは,手作
りの最高品質と同等なものが連続的に生産し得られるな
ど優れた特徴を有するものである。
In addition, in the viscous liquid inside the container that has been covered with a film, the coagulating agent, which is lime, gradually enters the particles.
Since the heat treatment is carried out in this state, solidification is completed and a product in a closed state with manna particles scattered therein is obtained. As described above, according to the present invention, by stirring and kneading konjac raw materials in the same tank, it is possible to produce a raw material that can be made into a paste and coagulated by mixing with lime water.6 Particularly. The vertical wing 6 oblique wing and horizontal wing constituting the frame-shaped wing 6 each have a swept angle, and
Stirring of raw materials is achieved by installing one screw blade on the frame-shaped blade. The kneading action is carried out effectively, and the tactile action of the raw material is actively carried out, and furthermore, the tactile action of the raw material is circulated by the pump and pipe 13. Furthermore, since the tactile effect of the raw material is increased, the obtained konjac has excellent characteristics such as being able to continuously produce the highest quality of handmade konnyaku.

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

第1図は一部切欠正面図6第2図は同上要部の縦断正面
図6第3図は第2図A−A線の断面図,第4図は第2図
B−B線の断面図,第5図は自動連続包装装置と組み合
わせた伏態の平面図である。
Fig. 1 is a partially cutaway front view 6 Fig. 2 is a longitudinal sectional front view of the main parts of the above 6 Fig. 3 is a cross-sectional view taken along line A-A in Fig. 2, Fig. 4 is a cross-sectional view taken along line B-B in Fig. 2 FIG. 5 is a plan view of the automatic continuous packaging device in a laid-down state.

Claims (1)

【特許請求の範囲】[Claims] 1 (イ)円筒漏斗形状をなした上部を開放せる槽の内
部中心軸線方向に、上端に伝動部を有する回転軸を配設
し、(ロ)該回転軸に、上記槽の内壁面に近接する垂直
翼3、斜翼4、および水平翼5とからなる枠状翼6をと
りつけるとともに、上記各翼3、4、5に、原料を攪拌
練合するための後退角を夫々もたせ、(ハ)上記枠状翼
6に、上記回転軸と平行な自転公転するスクリュー翼7
を設け、(ニ)また、上記槽の下側部に、パイプ11を
介してポンプ12を接続し、このポンプの吐出端に、切
換バルブ14を介して槽内原料を、槽の上部に開放され
た出口から触気させながら槽内に循環せしめるパイプ1
3、及び、上記切換バルブ14を介して槽内原料を、定
量充填機のホッパーに供給するパイプ15を設けたこと
を特徴とするコンニヤクの製造装置。
1. (a) A rotating shaft having a transmission part at the upper end is disposed in the direction of the internal central axis of a cylindrical funnel-shaped tank with an open top, and (b) the rotating shaft is located close to the inner wall surface of the tank. A frame-shaped blade 6 consisting of a vertical blade 3, an oblique blade 4, and a horizontal blade 5 is attached, and each of the blades 3, 4, and 5 is provided with a receding angle for stirring and kneading the raw materials. ) A screw blade 7 that rotates and revolves parallel to the rotation axis is attached to the frame-shaped blade 6.
(d) Also, a pump 12 is connected to the lower part of the tank via a pipe 11, and the raw material in the tank is released to the upper part of the tank via a switching valve 14 at the discharge end of this pump. Pipe 1 that circulates the air into the tank from the outlet
3. A konjac manufacturing apparatus characterized by being provided with a pipe 15 for supplying the raw material in the tank to a hopper of a quantitative filling machine via the switching valve 14.
JP55013392A 1980-02-05 1980-02-05 Konjac manufacturing equipment Expired JPS5925592B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55013392A JPS5925592B2 (en) 1980-02-05 1980-02-05 Konjac manufacturing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55013392A JPS5925592B2 (en) 1980-02-05 1980-02-05 Konjac manufacturing equipment

Publications (2)

Publication Number Publication Date
JPS56109566A JPS56109566A (en) 1981-08-31
JPS5925592B2 true JPS5925592B2 (en) 1984-06-19

Family

ID=11831828

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55013392A Expired JPS5925592B2 (en) 1980-02-05 1980-02-05 Konjac manufacturing equipment

Country Status (1)

Country Link
JP (1) JPS5925592B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6019438A (en) * 1983-07-11 1985-01-31 増田 文彦 Stirring apparatus of viscous substance such as food dough

Also Published As

Publication number Publication date
JPS56109566A (en) 1981-08-31

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