JPH0191818A - Continuous boiling apparatus - Google Patents
Continuous boiling apparatusInfo
- Publication number
- JPH0191818A JPH0191818A JP62248478A JP24847887A JPH0191818A JP H0191818 A JPH0191818 A JP H0191818A JP 62248478 A JP62248478 A JP 62248478A JP 24847887 A JP24847887 A JP 24847887A JP H0191818 A JPH0191818 A JP H0191818A
- Authority
- JP
- Japan
- Prior art keywords
- steaming
- pipe
- steam
- raw materials
- raw material
- 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
Links
- 238000009835 boiling Methods 0.000 title description 4
- 238000010025 steaming Methods 0.000 claims abstract description 68
- 239000002994 raw material Substances 0.000 claims abstract description 59
- 238000005192 partition Methods 0.000 claims abstract description 19
- 239000006260 foam Substances 0.000 claims 1
- 235000013527 bean curd Nutrition 0.000 abstract description 13
- 238000002156 mixing Methods 0.000 abstract description 4
- 238000010793 Steam injection (oil industry) Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract description 3
- 239000001397 quillaja saponaria molina bark Substances 0.000 abstract description 3
- 229930182490 saponin Natural products 0.000 abstract description 3
- 150000007949 saponins Chemical class 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract description 2
- 102000004169 proteins and genes Human genes 0.000 abstract description 2
- 108090000623 proteins and genes Proteins 0.000 abstract description 2
- 230000015556 catabolic process Effects 0.000 abstract 1
- 238000006731 degradation reaction Methods 0.000 abstract 1
- 238000005188 flotation Methods 0.000 abstract 1
- 235000010469 Glycine max Nutrition 0.000 description 5
- 244000068988 Glycine max Species 0.000 description 5
- 239000004480 active ingredient Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 235000013322 soy milk Nutrition 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000014347 soups Nutrition 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は豆腐原料やスープの高粘度状物等のための連続
蒸煮装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a continuous steaming apparatus for high viscosity materials such as tofu raw materials and soups.
(従来の技術とその問題点)
水に漬けた大豆をすり潰した呉や粉末状大豆や圧扁大豆
に加水したもの等の豆腐の原料を室温から100℃位ま
で徐々に均一に加熱処理することを一般に蒸煮と称して
いる。(Prior art and its problems) Gradually and uniformly heat-processing raw materials for tofu, such as mashed soybeans soaked in water, powdered soybeans, and compressed soybeans with water added, from room temperature to about 100°C. is generally called steaming.
従来、多くの蒸煮装置または加熱装置が使用されている
。例えば、特公昭61−22940号に示す装置はその
一例であり、該装置の主要構成要素は、スクリニーコン
ベヤ状の邪魔板であるため、蒸煮管に供給された原料は
その粒子間の相互位置関係をほぼそのままに、すなわち
撹拌・混合作用を受けることなく搬送される。そのため
、蒸気筒の近くの呉と、離れた位置にある呉とでは蒸煮
程度に差が生じ、煮ムラが発生し、そのため良好な食感
と組織の豆腐が得られない。また、蒸煮管内が密閉系で
あり、すなわち呉送出口が上端部に位置しており、しか
も別途泡出管が存在しないため、サポニン等の苦味成分
を泡の発生、排出によって除去し得ない欠点がある。Conventionally, many steaming or heating devices are used. For example, the device shown in Japanese Patent Publication No. 61-22940 is one such example, and the main component of this device is a screeny conveyor-like baffle plate, so that the raw material supplied to the steaming tube is It is transported with almost the same relationship, that is, without being subjected to stirring or mixing. As a result, there is a difference in the degree of steaming between the Kure near the steam cylinder and the Kure located further away, resulting in uneven boiling, making it impossible to obtain tofu with good texture and texture. Another disadvantage is that the inside of the steaming tube is a closed system, that is, the soybean outlet is located at the upper end, and there is no separate bubble tube, so bitter components such as saponin cannot be removed by generating and discharging bubbles. There is.
また、特公昭46−2391号に示す他の従来公知の装
置においては、円筒釜内に邪魔板が存在しないため、円
筒釜内に供給された原料は何ら撹拌・混合されずに搬送
される。その結果、不均一な加熱状態となり、煮ムラが
生じると共に、蒸気噴出管より噴出した水蒸気が原料と
充分に混り合うことなしに泡を形成し、この泡が上方に
浮上し、空気抜き管を介し排出されるため加熱効率が低
下する欠点がある。Further, in another conventionally known apparatus shown in Japanese Patent Publication No. 46-2391, since there is no baffle plate in the cylindrical pot, the raw materials supplied into the cylindrical pot are transported without being stirred or mixed at all. As a result, uneven heating occurs, causing uneven boiling, and the steam ejected from the steam jet pipe does not mix sufficiently with the raw material, forming bubbles, which float upwards and cause the air vent pipe to flow. There is a drawback that heating efficiency decreases because the gas is discharged through the gas.
本発明はこのような現状に鑑みてなされたものであって
、装置内の煮ムラを解消し、豆腐等の原料内の苦味成分
を除去し、該原料の酸化と風味劣化を防止し、蒸煮の進
行に伴う温度上昇・泡の発生の増加によるオーバフロー
により有効成分の歩留りが低下するのを防止することが
できる連続蒸煮装置を提供することを目的とするもので
ある。The present invention was made in view of the current situation, and it eliminates uneven boiling in the device, removes bitter components in raw materials such as tofu, prevents oxidation and flavor deterioration of the raw materials, and improves steaming. It is an object of the present invention to provide a continuous steaming apparatus that can prevent the yield of active ingredients from decreasing due to overflow caused by a rise in temperature and an increase in the generation of bubbles as the process progresses.
(問題点を解決するための手段)
上述の目的を達成するために、本発明の連続蒸煮装置は
、蒸煮管と該蒸煮管の中を長手方向に延び多数の蒸気噴
出孔を有する蒸気噴出管とからなる縦型二重構造であり
、前記蒸煮管の軸線にほぼ垂直で一部に切欠部を有する
複数個の仕切板を該切欠部が相互に対向位置になるよう
配設して前記蒸煮管と前記蒸気噴射管の間をほぼ等間隔
に分割し、原料供給口を前記蒸煮管の下端部に設け、原
料送出口を前記蒸煮管の上端部より所定距離下方に設け
、且つ水蒸気及び泡の排出管を前記蒸煮管の上端部に連
通させて構成される。(Means for Solving the Problems) In order to achieve the above-mentioned object, the continuous steaming apparatus of the present invention includes a steaming pipe and a steam jetting pipe extending longitudinally inside the steaming pipe and having a large number of steam jetting holes. It has a vertical double structure consisting of a plurality of partition plates that are substantially perpendicular to the axis of the steaming tube and have cutouts in some parts, and are arranged so that the cutouts are in opposing positions to each other. The space between the pipe and the steam injection pipe is divided at approximately equal intervals, a raw material supply port is provided at the lower end of the steaming pipe, a raw material delivery port is provided a predetermined distance below the upper end of the steaming pipe, and water vapor and bubbles are provided. A discharge pipe is connected to the upper end of the steaming pipe.
(実施例)
図面に基づいて本発明の実施例に係る豆腐原料用の連続
蒸煮装置を説明する。頂板と底板を有する縦型の円筒状
蒸煮管1は、その内部にこれと同一軸線に蒸気噴出管3
が設けられた二重構造となっている。該蒸気噴出管はそ
の外周壁に多数の蒸気噴出孔2を有する。(Example) A continuous steaming apparatus for tofu raw materials according to an example of the present invention will be described based on the drawings. A vertical cylindrical steaming pipe 1 having a top plate and a bottom plate has a steam jetting pipe 3 inside thereof along the same axis.
It has a double structure with The steam jet pipe has a large number of steam jet holes 2 on its outer peripheral wall.
前記蒸煮管1と前記噴出管3との間の空間は複数枚の仕
切板5によって複数、例えば12のチャンバー8に分割
されている。ここで、仕切り板5の配置間隔と蒸煮管の
内径との比を0.5:1ないし0.9:1とすると、豆
腐原料の撹拌混合効率を高めることができる。該仕切板
5は前記両管の軸線に対しほぼ垂直で且つほぼ等間隔に
設けられている。前記噴出管3は各仕切板5の孔6を貫
通している。The space between the steaming pipe 1 and the ejection pipe 3 is divided into a plurality of chambers 8, for example twelve, by a plurality of partition plates 5. Here, if the ratio between the arrangement interval of the partition plates 5 and the inner diameter of the steaming tube is set to 0.5:1 to 0.9:1, the stirring and mixing efficiency of the tofu raw materials can be increased. The partition plates 5 are provided substantially perpendicularly to the axes of both tubes and at substantially equal intervals. The jet pipe 3 passes through a hole 6 in each partition plate 5.
前記仕切板5は蒸煮管1の内径に等しい円板で、第3図
に示すように、直線状に切断した切欠部7を備えている
。蒸煮管1の断面積と切欠部7の面積との比は、1:O
,’05ないし1:0.25であることが好ましい。第
2図に示すように、前記切欠部7は上から右側、次は左
側と互い違いに配置され、豆腐の原料が蒸煮管の内部を
仕切板によって曲りくねって流動するようになっている
。なお、切欠部は円板を直線状に切欠くことに限られず
、例えば円板に円孔を偏心させて設けてもよい。The partition plate 5 is a circular plate having an inner diameter equal to the inner diameter of the steaming tube 1, and is provided with a notch 7 cut into a straight line, as shown in FIG. The ratio of the cross-sectional area of the steaming tube 1 to the area of the notch 7 is 1:O.
, '05 to 1:0.25. As shown in FIG. 2, the notches 7 are arranged alternately from the top to the right, then to the left, so that the tofu raw material flows through the inside of the steaming tube by winding through the partition plate. Note that the cutout portion is not limited to a linear cutout in the disk, and may be formed by, for example, providing an eccentric circular hole in the disk.
前記蒸気噴出管3は、蒸煮管1の底板を貫通して蒸気供
給管4に連結され、ここから蒸気が供給される。また、
蒸煮管1の底板に原料供給口9が設けられ、該原料供給
口に原料圧送ポンプ(図示せず)から豆腐の原料が供給
管11及び三方バルブ10を通じて送り込まれる。The steam ejection pipe 3 passes through the bottom plate of the steaming pipe 1 and is connected to a steam supply pipe 4, from which steam is supplied. Also,
A raw material supply port 9 is provided in the bottom plate of the steaming tube 1, and raw materials for tofu are fed into the raw material supply port from a raw material pressure pump (not shown) through a supply pipe 11 and a three-way valve 10.
さらに、前記蒸煮管1の上方側面に原料送出口12があ
けられている。該原料送出口12は蒸煮管の上端部より
所定距離り、、 h2、h5、h、・・・・下方に位置
している。第1図に示すように、複数個の蒸煮管1を並
置して直列に接続した場合、作業工程が遅くなるほどす
なわち後工程になるほど前述の所定距離が大きくなって
いる。なお、蒸煮管1の高さと上記距離h1、h2、h
3、h4・・・・の比は、1:0.05ないし1 :
0.5であることが好ましい。第1図において右から左
に進むにつれて後工程となる。前記原料送出口12は、
連結管すなわち、原料送出管13により前記原料供給管
11に連結されている。Furthermore, a raw material delivery port 12 is provided on the upper side surface of the steaming tube 1 . The raw material outlet 12 is located at a predetermined distance below the upper end of the steaming tube. As shown in FIG. 1, when a plurality of steaming tubes 1 are arranged side by side and connected in series, the above-mentioned predetermined distance increases as the working process becomes slower, that is, the later the process becomes. In addition, the height of the steaming pipe 1 and the above distances h1, h2, h
3. The ratio of h4... is 1:0.05 to 1:
Preferably it is 0.5. In FIG. 1, the process progresses from right to left toward subsequent steps. The raw material delivery port 12 is
It is connected to the raw material supply pipe 11 by a connecting pipe, that is, a raw material delivery pipe 13 .
蒸煮管1の頂板に設けた孔に排出管16を連結し、該蒸
煮管上方部より排出された水蒸気及び泡が前記排出管1
6に連結した凝縮器17に運ばれ、凝縮されて排出され
る。該1!縮器17の上部に凝縮用の冷却水の供給管1
4が連結されている。A discharge pipe 16 is connected to a hole provided in the top plate of the steaming pipe 1, and water vapor and bubbles discharged from the upper part of the steaming pipe are discharged from the discharge pipe 1.
6 and is condensed and discharged. Part 1! A cooling water supply pipe 1 for condensation is installed in the upper part of the condenser 17.
4 are connected.
以上の構成になる本発明の連続蒸煮装置は次のように作
動する。図面に示す連続蒸煮装置は、4本の蒸煮管1を
並置し、原料供給管11は蒸煮管毎に設けた三方バルブ
を介して直列に接続されている。また、排出管16もす
べての蒸煮管について直列に接続されている。The continuous steaming apparatus of the present invention having the above structure operates as follows. In the continuous steaming apparatus shown in the drawing, four steaming tubes 1 are arranged side by side, and the raw material supply tubes 11 are connected in series through a three-way valve provided for each steaming tube. Further, the discharge pipes 16 are also connected in series for all the steaming pipes.
蒸気供給管4によって供給される蒸気は蒸気噴出管3か
ら蒸煮管1の内部に噴出されてその内部を所定温度に上
昇させる。この温度設定は別途設けられた温度制御装置
からの動作信号に応動して開閉する、蒸気供給管4の途
中に設置さた電磁弁により行われる。Steam supplied by the steam supply pipe 4 is ejected from the steam jet pipe 3 into the inside of the steaming pipe 1 to raise the inside temperature to a predetermined temperature. This temperature setting is performed by a solenoid valve installed in the middle of the steam supply pipe 4, which opens and closes in response to an operation signal from a separately provided temperature control device.
豆腐の原料が、第1図に矢印Aで示すように、原料圧送
ポンプから最初の蒸煮管の三方バルブ10に給送される
。該三方バルブを調節して上方向ポートを解放し、流入
側横方向ポートを解放し、流出側横方向ポートを閉鎖す
る。かくすることによって前記原料が蒸煮管1に供給さ
れ、その中において圧送ポンプによる下方からの圧送力
と、蒸気噴射孔2から噴射される高圧蒸気によって各チ
ャンバー8内にて充分に混合され、更に仕切板5に衝突
し、拡散されて混合度合を高め、その結果全体に亘り均
一に加熱された後、矢印已に示すように原料送出口12
から連結管13を通り、次の三方バルブを通って次の蒸
煮管に供給される。The raw material for tofu is fed from the raw material pressure pump to the three-way valve 10 of the first steaming pipe, as shown by arrow A in FIG. The three-way valve is adjusted to open the upper port, open the inlet lateral port, and close the outlet lateral port. As a result, the raw materials are supplied to the steaming pipe 1, where they are thoroughly mixed in each chamber 8 by the force of the pressure pump from below and the high pressure steam injected from the steam injection holes 2, and further After colliding with the partition plate 5, being diffused and increasing the mixing degree, and as a result, being heated uniformly over the entire area, the raw material is transferred to the raw material delivery port 12 as shown by the arrow.
From there, it passes through the connecting pipe 13, passes through the next three-way valve, and is supplied to the next steaming pipe.
なお、この時蒸煮管内の原料の液面は原料送出口12の
ほぼ下端にあり、同液面上方の空間には原料から発生し
た泡(内部水蒸気)が充満しており、これらの泡はオー
バフロー現象にて矢印Cに示すよう排出管16から排出
され、凝縮器17を通じて、矢印りで示すよう凝縮・排
出される。なお、豆腐原料の温度上昇の状況は、第1な
いし第4蒸煮管の原料送出口で測定すると、それぞれの
位置で、例えば50℃、75℃、90℃、100℃であ
る。At this time, the liquid level of the raw material in the steaming tube is almost at the lower end of the raw material outlet 12, and the space above the liquid level is filled with bubbles (internal steam) generated from the raw material, and these bubbles are caused by overflow. Due to this phenomenon, it is discharged from the discharge pipe 16 as shown by the arrow C, and is condensed and discharged through the condenser 17 as shown by the arrow. Note that the temperature rise of the tofu raw material is, for example, 50°C, 75°C, 90°C, and 100°C at each position when measured at the raw material outlet of the first to fourth steaming tubes.
以上のように、原料は各蒸煮管において連続的に加熱・
蒸煮・圧送され、最終的に約100℃に均一に加熱され
た原料は矢印Eに示すよう、次のオカラ・豆乳分離工程
等へ搬送される。このようにして呉を連続的に蒸煮する
ことができる。As mentioned above, the raw materials are continuously heated and heated in each steaming tube.
The raw material, which is steamed, pressure-fed, and finally uniformly heated to approximately 100°C, is transported to the next okara/soy milk separation process, etc., as shown by arrow E. In this way, gou can be steamed continuously.
(発明の効果)
以上説明したような構成を有する本発明の連続蒸煮装置
は次のような効果を有する。(Effects of the Invention) The continuous steaming apparatus of the present invention having the configuration as described above has the following effects.
前記仕切板により分割形成された各チャンバーにおいて
、該仕切板の切欠部から圧送される原料と噴出蒸気によ
って、既にそのチャンバーに存在していた原料が撹拌さ
れ蒸煮が均−且つ充分に行われるので煮ムラが生じない
効果がある。また、仕切板によって噴出水蒸気が泡を形
成し蒸煮管の上方に浮上することを抑制し、水蒸気と原
料を充分に接触混合させるので加熱効率も向上する。In each chamber divided by the partition plate, the raw material already present in the chamber is stirred by the raw material and jetted steam pumped from the notch of the partition plate, and steaming is performed evenly and sufficiently. This has the effect of preventing uneven cooking. In addition, the partition plate prevents the ejected steam from forming bubbles and floating above the steaming tube, and the steam and raw materials are sufficiently contacted and mixed, thereby improving heating efficiency.
さらに、前記仕切板により原料く豆乳・呉)中に含まれ
る蛋白等の有効成分からなる泡の形成と上方浮上を抑制
し、有効成分が排水管から出るのを防ぐ。サポニン等の
苦味成分からなる泡は安定性が高いので前記仕切板によ
って上方への浮上・排出は妨げられないので苦味成分を
有効に除去できる効果がある。Further, the partition plate suppresses the formation and upward floating of bubbles consisting of active ingredients such as proteins contained in the raw materials (soy milk, soy milk, soybean paste), and prevents the active ingredients from coming out of the drain pipe. Since the bubbles made of bitter components such as saponin are highly stable, the partition plate does not prevent them from floating upward and being discharged, so that the bitter components can be effectively removed.
原料送出口を所定の位置に設けることにより、蒸煮管内
の原料の上方に所定の空間を形成し、ここに泡を存在さ
せることにより外気と原料の接触度合を低減させて豆腐
原料の酸化や風味劣化を防止することができる効果があ
る。By providing the raw material outlet at a predetermined position, a predetermined space is formed above the raw material in the steaming tube, and by creating bubbles in this space, the degree of contact between the outside air and the raw material is reduced, and the oxidation and flavor of the tofu raw material are reduced. It has the effect of preventing deterioration.
原料の蒸煮が進むに従い、温度が上昇し、泡の発生が増
加し、オーバーフローが起り、このため有効成分の歩留
りが低下する従来の欠点を解決するため、本発明では後
工程の蒸煮管はど原料送出口の位置を低くしているので
、すなわち泡の存在し得る容積を大きくしているのでオ
ーバフローの発生がなく、従って歩留りの低下を生じな
い。In order to solve the conventional drawbacks that as the steaming of raw materials progresses, the temperature rises, the generation of bubbles increases, and overflow occurs, which reduces the yield of active ingredients. Since the position of the raw material delivery port is set low, that is, the volume in which bubbles can exist is increased, overflow does not occur, and therefore, the yield does not decrease.
第1図は本発明の連続蒸煮装置の正面図、第2図は1部
を断面にした同側面図、第3図は仕切板の平面図である
。
1・・・・蒸煮管・
2・・・・蒸気噴出孔
3・・・・蒸気噴出管
4・・・・蒸気供給管
5・・・・仕切板
6・・・・孔
7・・・・切欠部
8・・・・チャンバー
9・・・・原料供給口
10・・・・三方バルブ
11・・・・原料供給管
12・・・・原料送出口
13・・・・連結管
14・・・・冷却水供給管
16・・・・排出管
17・・・・凝縮管
第1図
第2図FIG. 1 is a front view of the continuous steaming apparatus of the present invention, FIG. 2 is a partially sectional side view of the same, and FIG. 3 is a plan view of a partition plate. 1... Steaming pipe 2... Steam jetting hole 3... Steam jetting pipe 4... Steam supply pipe 5... Partition plate 6... Hole 7... Notch 8...Chamber 9...Raw material supply port 10...Three-way valve 11...Raw material supply pipe 12...Raw material outlet 13...Connecting pipe 14...・Cooling water supply pipe 16... Discharge pipe 17... Condensing pipe Figure 1 Figure 2
Claims (2)
多数の蒸気噴出孔(2)を有する蒸気噴出管(3)とか
ら成る縦型二重構造の連続蒸煮装置において、 一部に切欠部(7)を有し前記蒸煮管の軸線にほぼ垂直
な複数枚の仕切板(5)の隣り合うものを該切欠部が相
互に対向位置になるよう配設して前記蒸煮管(1)と前
記蒸気噴出管(3)との間をほぼ等間隔に分割し、原料
供給口(9)を前記蒸煮管(1)の下端部に設け、原料
送出口(12)を前記蒸煮管(1)の上端部より所定距
離下方に設け、且つ水蒸気及び泡の排出管(16)を前
記蒸煮管(1)の上端部に連通させたことを特徴とする
連続蒸煮装置。(1) A vertical double-structured continuous steaming device consisting of a steaming pipe (1) and a steam jetting pipe (3) extending longitudinally inside the steaming pipe and having a large number of steam jetting holes (2), A plurality of adjacent partition plates (5) each having a notch (7) in a part and substantially perpendicular to the axis of the steaming tube are arranged so that the notches face each other. The space between the pipe (1) and the steam jetting pipe (3) is divided into approximately equal intervals, the raw material supply port (9) is provided at the lower end of the steaming pipe (1), and the raw material delivery port (12) is provided at the lower end of the steaming pipe (1). A continuous steaming device, characterized in that it is provided a predetermined distance below the upper end of the steaming pipe (1), and a steam and foam discharge pipe (16) is communicated with the upper end of the steaming pipe (1).
原料送出口(12)が後工程になるにつれ前記蒸煮管(
1)の上端部より漸次低くなるように配設されているこ
とを特徴とする特許請求の範囲第(1)項記載の連続蒸
煮装置。(2) A plurality of the steaming pipes (1) are connected in series, and the steaming pipes (1) are
1) The continuous steaming apparatus according to claim 1, wherein the continuous steaming apparatus is arranged so as to be gradually lower than the upper end.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62248478A JP2544158B2 (en) | 1987-10-01 | 1987-10-01 | Continuous steaming equipment |
KR1019880011500A KR910000141B1 (en) | 1987-09-07 | 1988-09-06 | Continuous digesting apparatus |
FR8811705A FR2619993B1 (en) | 1987-09-07 | 1988-09-07 | CONTINUOUS DIGESTION APPARATUS, PARTICULARLY BY STEAM COOKING OF FOOD PRODUCTS |
GB8820932A GB2209463B (en) | 1987-09-07 | 1988-09-07 | Continuous digesting apparatus |
US07/241,623 US4884498A (en) | 1987-09-07 | 1988-09-07 | Continuous digesting apparatus |
CN88106499A CN1027571C (en) | 1987-09-07 | 1988-09-07 | Continuous digesting apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62248478A JP2544158B2 (en) | 1987-10-01 | 1987-10-01 | Continuous steaming equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0191818A true JPH0191818A (en) | 1989-04-11 |
JP2544158B2 JP2544158B2 (en) | 1996-10-16 |
Family
ID=17178747
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62248478A Expired - Lifetime JP2544158B2 (en) | 1987-09-07 | 1987-10-01 | Continuous steaming equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2544158B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012135228A (en) * | 2010-12-24 | 2012-07-19 | Marui Kogyo Kk | Continuous boiling pot |
-
1987
- 1987-10-01 JP JP62248478A patent/JP2544158B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012135228A (en) * | 2010-12-24 | 2012-07-19 | Marui Kogyo Kk | Continuous boiling pot |
Also Published As
Publication number | Publication date |
---|---|
JP2544158B2 (en) | 1996-10-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4534283A (en) | Method and apparatus for manufacturing bean curd | |
JPH0191818A (en) | Continuous boiling apparatus | |
KR910000141B1 (en) | Continuous digesting apparatus | |
JP4386920B2 (en) | How to boil wort | |
CN109152496A (en) | The output device of milk frothing device | |
JP2544159B2 (en) | Continuous steaming equipment | |
WO1999031998A1 (en) | Boiling pot | |
CN212814082U (en) | Automatic flow control and connection type soybean milk returning system for bean product production | |
CN211486617U (en) | Extraction device of fermented wine raw materials | |
KR200196421Y1 (en) | A manufacturing machine of powdeved bean cuid | |
JP3004981B1 (en) | Boiled pot | |
CN219680330U (en) | Steaming tool and cooking equipment using same | |
JP2973199B1 (en) | Continuous soybean boiling device | |
JPS61257153A (en) | Heater for making 'tofu' (bean-curd) | |
JPS6221497B2 (en) | ||
CN220477423U (en) | Cooking utensil | |
JPH01193502A (en) | Steam character converter | |
JP4570561B2 (en) | Boiled pot equipment | |
JPS6213506Y2 (en) | ||
CN216018940U (en) | Ice cream basin puffing device | |
RU2786544C2 (en) | Capsule with foaming agent | |
SU1054655A1 (en) | Heat exchanger | |
KR200293035Y1 (en) | Multi stage dryer of cheese whey | |
CN208624515U (en) | It is a kind of for producing the sugar boiler of candy | |
JPH02227039A (en) | Continuous type boiling and aging vessel |