JPS5826942B2 - Method for producing pressure-bubbled confectionery granules and pressure-bubbled confectionery liquid coagulation/grinding container used therein - Google Patents
Method for producing pressure-bubbled confectionery granules and pressure-bubbled confectionery liquid coagulation/grinding container used thereinInfo
- Publication number
- JPS5826942B2 JPS5826942B2 JP55021992A JP2199280A JPS5826942B2 JP S5826942 B2 JPS5826942 B2 JP S5826942B2 JP 55021992 A JP55021992 A JP 55021992A JP 2199280 A JP2199280 A JP 2199280A JP S5826942 B2 JPS5826942 B2 JP S5826942B2
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- Japan
- Prior art keywords
- container
- confectionery
- coagulation
- pressure
- pulverization
- 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
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- Confectionery (AREA)
- Grain Derivatives (AREA)
Description
【発明の詳細な説明】
この発明は、圧力ガスを気泡状に混入した菓子粒の製造
方法、及びそれに使用される凝固粉砕容器に関し、菓子
液の冷却能率をあげることにより、圧力気泡入り菓子粒
を高能率に製造するようにしたものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing confectionery grains containing bubbles of pressure gas, and a coagulation and crushing container used therein. It is designed to manufacture with high efficiency.
一般にこの種の菓子は、溶融状の菓子原液を高圧のガス
雰囲気中で攪拌し、菓子原液中に高圧ガス(例えば炭酸
ガス)を気泡状に混入させ、気泡が混入している状態の
菓子液を冷却凝固させることにより製造されているビ
ところがこの場合、気泡混入菓子液の冷却凝固工程が、
撹拌による菓子原液への圧力ガス混入工程やその他の工
程に較べて格段に時間がかかり、この冷却工程が製造時
間の短縮化を阻害していた。Generally, this type of confectionery is made by stirring a molten confectionery stock solution in a high-pressure gas atmosphere, and then mixing high-pressure gas (e.g. carbon dioxide gas) into the confectionery stock solution in the form of bubbles. However, in this case, the cooling and solidification process of the aerated confectionery liquid is
This cooling process has been a hindrance to shortening the manufacturing time, as it takes much more time than other processes such as mixing pressurized gas into the confectionery stock solution by stirring.
本発明はこのような点に鑑み提案されたもので、気泡混
入後の菓子液を凝固・粉砕容器内に移送し、この気泡混
入菓子液を収容した状態の凝固・粉砕容器を気泡混入容
器から切離して冷却装置に移送して強制的に冷却させる
ようにしたことを特徴とするものである。The present invention has been proposed in view of these points, and involves transferring the confectionery liquid with air bubbles mixed into it into a coagulation/pulverization container, and then transferring the coagulation/crushing container containing the air bubbles mixed confectionery liquid from the air bubble mixing container. It is characterized in that it is separated and transferred to a cooling device to be forcibly cooled.
以下、本発明方法の実施に使用する装置の一例を図面に
基づき説明する。Hereinafter, an example of an apparatus used to carry out the method of the present invention will be explained based on the drawings.
第1図は気泡入り菓子製造装置の概略正面図であり、図
において符号1は熔融状態の菓子原液にガスを混入させ
る気泡混入容器、2は気泡混入容器1の下側に配置され
た気泡混入菓子液を凝固・粉砕する凝固・粉砕容器、3
は気泡混入容器1と凝固・粉砕容器とを連結する菓子液
流入口であり、気泡混入容器1と凝固・粉砕容器2とは
それぞれ骨枠部材4に支持されている。FIG. 1 is a schematic front view of an aerated confectionery manufacturing apparatus. In the figure, reference numeral 1 denotes an air bubble mixing container for mixing gas into the molten confectionery stock solution, and 2 indicates an air bubble mixing container disposed below the air bubble mixing container 1. A coagulating and crushing container for coagulating and crushing confectionery liquid, 3
is a confectionery liquid inlet that connects the air bubble mixing container 1 and the coagulation/pulverization container, and the air bubble mixing container 1 and the coagulation/grinding container 2 are each supported by a frame member 4.
気泡混入容器1内の気泡混入室5は、上蓋6で締め切ら
れて、気密に保たれる。The air bubble mixing chamber 5 in the air bubble mixing container 1 is closed off with an upper lid 6 and kept airtight.
気泡混入容器1の上部の取付鍔7に菓子原液人口8と気
体注入口9とが明けられる。A confectionery concentrate 8 and a gas injection port 9 are provided in the mounting collar 7 at the top of the air bubble mixing container 1.
菓子原液人口8は電磁弁10゜供給管11.及びポンプ
12を介して菓子原液製造釜13に連結され、気体注入
口9はガス管14゜電磁弁15及び圧力設定弁17を介
してボンベ19に接続される。Confectionery stock solution population 8 is solenoid valve 10° supply pipe 11. The gas inlet 9 is connected to a cylinder 19 via a gas pipe 14, a solenoid valve 15, and a pressure setting valve 17.
20は圧抜き電磁弁である。気泡混入室5に気泡混入用
回転攪拌羽根21が収容される。20 is a pressure relief solenoid valve. A rotating stirring blade 21 for mixing air bubbles is housed in the air bubble mixing chamber 5 .
この攪拌羽根21は、筒軸22の下半部から羽根板23
を放射状に連出させ、各羽根板23に押上げ角θをもた
せである。This stirring blade 21 extends from the lower half of the cylinder shaft 22 to the blade plate 23.
are made to extend radially, and each blade plate 23 is made to have a pushing-up angle θ.
各羽根板お及び気泡混入室5の各底面24.25が中央
下りの傾斜面に形成され、気泡混入室5の周面の下部2
6が少し細く絞られる。Each of the blade plates and the bottom surfaces 24 and 25 of the air bubble mixing chamber 5 are formed as inclined surfaces downward from the center, and the lower part 2 of the circumferential surface of the air bubble mixing chamber 5
6 is narrowed down a little.
攪拌羽根18は入力軸27.■ベルト伝動装置28を介
してモータ29に連動連結される。The stirring blade 18 is connected to the input shaft 27. (2) Interlockingly connected to a motor 29 via a belt transmission device 28.
入力軸27は上蓋6上に固定の軸受30に枢支されて、
メカニカルシール31で封止され、その軸下端に攪拌羽
根210筒軸22の上端が外嵌固定される。The input shaft 27 is pivotally supported on a bearing 30 fixed on the top cover 6,
It is sealed with a mechanical seal 31, and the upper end of the stirring blade 210 and the cylindrical shaft 22 are externally fitted and fixed to the lower end of the shaft.
モータ29は縦骨枠4の上部に固定のモータ取付台32
に固定される。The motor 29 is mounted on a motor mounting base 32 fixed to the upper part of the vertical frame 4.
Fixed.
気泡混入容器1の外周面及び下面が蒸気保温室33で取
囲まれている。The outer peripheral surface and lower surface of the bubble-containing container 1 are surrounded by a steam insulating chamber 33.
蒸気保温室33は、検温器34に検温され、その出力信
号で制御装置35が電磁弁36を開閉制御して蒸気の供
給量を自動調節する事により所定の温度に保たれる。The temperature of the steam insulating chamber 33 is measured by a thermometer 34, and a control device 35 uses the output signal to control the opening and closing of a solenoid valve 36 to automatically adjust the amount of steam supplied, thereby maintaining the temperature at a predetermined temperature.
気泡混入容器1の底壁中央に気泡混入菓子液の取出口3
7が形成してあシ、各凝固・粉砕容器2の土壁中央に開
口させた気泡混入菓子液の取入口38に菓子液導出管3
を介して連通させである。There is an outlet 3 for the air-filled confectionery liquid in the center of the bottom wall of the air-filled container 1.
7 is formed, and a confectionery liquid outlet pipe 3 is connected to the intake port 38 for the aerated confectionery liquid opened in the center of the earthen wall of each coagulation/pulverization container 2.
It is communicated through.
この菓子液導出路3は、導通管40と2個の仕切弁4L
42.及び両仕切弁41・42間に位置させた接続管4
3で構成されている。This confectionery liquid outlet path 3 is connected to a conduit pipe 40 and two gate valves 4L.
42. and a connecting pipe 4 located between both gate valves 41 and 42
It consists of 3.
連通管40.第1仕切弁41及び接続管43はこの間で
菓子液が凝固することがないように蒸気保温室44で取
囲まれて訃り、この蒸気保温室44は前記気泡混入容器
1の蒸気保温室33と連通して、共通の蒸気で保温され
るようになっている。Communication pipe 40. The first gate valve 41 and the connecting pipe 43 are surrounded by a steam insulating chamber 44 so that the confectionery liquid does not solidify between them. They are connected to each other and are kept warm by common steam.
また、接続管43と第2仕切弁42との間はボルトナツ
ト45により着脱自在に接続されている。Further, the connection pipe 43 and the second gate valve 42 are detachably connected by a bolt nut 45.
な釦、接続管43と第2仕切弁42との接続方法として
は、ボルトナンドの他に、クランプやVバンドによる締
込み、あるいは、油圧シリンダにより凝固・粉砕容器2
を押し上げ、この押上げ力により圧接させることなども
考えられる。The connecting method for connecting the connecting pipe 43 and the second gate valve 42 is by tightening with a clamp or V band, or by tightening the coagulation/pulverization container 2 with a hydraulic cylinder.
It is also conceivable to push up the material and use this pushing up force to bring the material into pressure contact.
気泡混入容器1内で圧力ガスを気泡状に混入した菓子液
は菓子液導出路3を通って気泡混入容器1の下側に位置
する凝固・粉砕容器2内に選択的に注入されたのち、凝
固・粉砕容器2は気泡容器1から切離されて冷却装置4
6に搬送される。The confectionery liquid mixed with bubbles of pressure gas in the bubble-mixing container 1 is selectively injected into the coagulation/pulverization container 2 located below the bubble-mixing container 1 through the confectionery liquid outlet passage 3. The coagulation/pulverization container 2 is separated from the bubble container 1 and placed in the cooling device 4.
6.
本発明の一つである凝固・粉砕容器2は、第4図に示す
ように、縦筒状の容器本体47の上面に気泡混入菓子液
取入口38が形成されるとともに、その底部を開放して
製品取り出し口48とし、この製品取出し口48を蓋4
9で密閉して、容器本体47内に凝固・粉砕室50が形
威しである。As shown in FIG. 4, the coagulation/grinding container 2 according to the present invention has an aerated confectionery liquid inlet 38 formed on the top surface of a vertically cylindrical container body 47, and has an open bottom. This product outlet port 48 is used as a product outlet port 48, and this product outlet port 48 is
9, and a coagulation/pulverization chamber 50 is formed within the container body 47.
そしてこの容器本体47の上部に加圧ガス流入口51が
形成してあり、この加圧ガス流入口51には遮断弁52
.電磁弁53.調圧弁54を介してボンベ19が接続し
てあり、遮断弁52と電磁弁53との間に着脱操作容易
な接続具55が装備しである。A pressurized gas inlet 51 is formed in the upper part of the container body 47, and a cutoff valve 52 is connected to the pressurized gas inlet 51.
.. Solenoid valve 53. A cylinder 19 is connected via a pressure regulating valve 54, and a connecting tool 55 that can be easily attached and detached is provided between the cutoff valve 52 and the electromagnetic valve 53.
また、凝固・粉砕室50と気泡混入容器1の気泡混入室
5とは均圧ライン56とで連通連結してあり、この均圧
ライン56中には2個の開閉弁57・58が介装してあ
り、両開閉弁57・58間に着脱操作容易な接続具59
が配置しである。Further, the coagulation/pulverization chamber 50 and the bubble mixing chamber 5 of the bubble mixing container 1 are connected to each other through a pressure equalization line 56, and two on-off valves 57 and 58 are interposed in the pressure equalization line 56. There is a connecting tool 59 between both on-off valves 57 and 58 that can be easily attached and detached.
is placed.
符号60は容器本#−47に付設した過圧逃し弁である
。Reference numeral 60 is an overpressure relief valve attached to container #-47.
容器本体47の製品取出し口48を閉塞する蓋49の内
面に、補強リブを兼ねる放射状フィン61を外周面に縦
向きに突設した冷却筒62が固着してあり、該冷却筒6
2の内部空間63は蓋49に形成した冷却水通孔64を
介して外気と連通させである。A cooling cylinder 62 having radial fins 61 that also serve as reinforcing ribs vertically protruding from the outer peripheral surface is fixed to the inner surface of the lid 49 that closes the product outlet 48 of the container body 47.
The internal space 63 of No. 2 is communicated with the outside air through a cooling water hole 64 formed in the lid 49.
次に、以上の構成からなる装置を用いて、本発明に係る
圧力気泡入り菓子粒を製造する方法の一実施手順例を説
明する。Next, an example of a procedure for producing pressure-bubbled confectionery grains according to the present invention using the apparatus configured as described above will be described.
菓子原液製造釜13から飴などの菓子原液を気泡混入容
器1内Vc6分目はど混入し、電磁弁15を開けて、ボ
ンベ19から気泡混入容器1内に炭酸ガス又は窒素ガス
等の無害ガスを30〜80kg/cIfL2に注入し保
持しながら、モータ29で攪拌羽根21を500〜12
00rpmで回転させる。Add confectionery concentrate such as candy from the confectionery concentrate production pot 13 into the bubble-mixing container 1 at the 6th minute Vc, open the solenoid valve 15, and pour harmless gas such as carbon dioxide or nitrogen gas into the bubble-mixing container 1 from the cylinder 19. While injecting and holding 30 to 80 kg/cIfL2, the stirring blade 21 is driven by the motor 29 to 500 to 12 kg/cIfL2.
Rotate at 00 rpm.
すると、気泡混入室5の上部空間内の圧力気体が菓子原
液内に気泡となって混入される。Then, the pressure gas in the upper space of the bubble mixing chamber 5 is mixed into the confectionery stock solution in the form of bubbles.
10分間はど攪拌すると圧力気体が菓子原液内に気泡状
に充分混入され、攪拌羽根21を停止する。After stirring for 10 minutes, the pressurized gas is sufficiently mixed into the confectionery concentrate in the form of bubbles, and the stirring blade 21 is stopped.
次いで電磁弁53・遮断弁52を開けて、ボンベ19か
らの圧力気体を凝固・粉砕室50内に注入して、凝固・
粉砕室50内を気泡混入室5とほぼ同圧にし、凝固・粉
砕容器2への仕切弁41・42を開くとともに均圧ライ
ン56の開閉弁5758を開くと、気泡混入菓子液が自
重により自然流下し凝固・粉砕容器2内へ移し替えられ
る。Next, the solenoid valve 53 and shutoff valve 52 are opened, and the pressure gas from the cylinder 19 is injected into the coagulation/pulverization chamber 50 to cause coagulation/pulverization.
When the inside of the crushing chamber 50 is made to have almost the same pressure as the air bubble mixing chamber 5, and the gate valves 41 and 42 to the coagulation and crushing container 2 are opened, and the on-off valve 5758 of the pressure equalization line 56 is opened, the confectionery liquid mixed with air bubbles will naturally flow under its own weight. It flows down and is transferred into the coagulation/pulverization container 2.
そして菓子液導入路30両仕切弁41・42を閉鎖した
のち、接続管43と第2仕切弁42との間の接続を切離
すとともに、均圧ライン56中の接続具59及び容器加
圧ラインの接続具55を切離し、凝固・粉砕容器2を冷
却装置46に搬送し、ここで凝固・粉砕容器2を冷却す
ることにより、気泡入り菓子液を圧力ガス雰囲気下で凝
固させ、内部に圧力気泡を内包する菓子固体な生成する
。After closing both the gate valves 41 and 42 of the confectionery liquid introduction path 30, the connection between the connecting pipe 43 and the second gate valve 42 is disconnected, and the connection fitting 59 in the pressure equalization line 56 and the container pressure line The connecting fitting 55 is disconnected, and the coagulation/pulverization container 2 is transferred to the cooling device 46, where the coagulation/pulverization container 2 is cooled to solidify the aerated confectionery liquid in a pressure gas atmosphere and create pressure bubbles inside. Produces a solid confectionery containing.
凝固・粉砕容器2を冷却装置46に搬送する手段として
は、容器2を搬送車で運ぶことや、レール上をスライド
させること、またコンベア上を移送させることなどが考
えられる。Possible means for transporting the coagulation/pulverization container 2 to the cooling device 46 include transporting the container 2 on a transport vehicle, sliding it on a rail, or transporting it on a conveyor.
また凝固・粉砕容器2を冷却する手段としては、容器2
を水槽内に浸漬させることや、容器2をシャワー状に形
成した冷水中をくぐらせることなどが考えられる。Further, as a means for cooling the coagulation/pulverization container 2, the container 2
Possible methods include immersing the container 2 in a water tank, or passing the container 2 through cold water formed in the shape of a shower.
容器2を水槽中に浸漬した場合には、冷却水が容器2の
底蓋49に形成した冷却水通孔64を通って冷却筒62
の内部空間63に流入し、容器2を内外両面から冷却す
る。When the container 2 is immersed in a water tank, the cooling water passes through the cooling water hole 64 formed in the bottom cover 49 of the container 2 and flows into the cooling tube 62.
, and cools the container 2 from both the inside and outside.
また、容器2をシャワー状の冷水をくぐらせる場合には
第6図に示すように冷却水導入管65を冷却筒62内に
突入させ、冷却水を冷却筒62の内部空間で噴水状に噴
出させて、容器2を内外両面から冷却する。In addition, when the container 2 is made to pass through a shower of cold water, the cooling water introduction pipe 65 is inserted into the cooling cylinder 62 as shown in FIG. The container 2 is cooled from both the inside and outside.
な釦冷却水導入管65は冷却筒62内にあらかじめ配置
しておいてもよい。The button cooling water introduction pipe 65 may be placed in the cooling cylinder 62 in advance.
冷却装置46で充分冷却された凝固・粉砕容器2は除湿
器66に搬入され、ここで均圧ライン56中の開閉弁5
7または、加圧ライン中の開閉弁52を開弁じ、凝固・
粉砕室50内の圧力を大気圧にまで低下させると、凝固
した気泡入り菓子固体は大きな気泡が破裂して5′b
そののち底蓋49を開いて容器本体47の製品取出し口
48を開放し、気泡入り菓子粒を除湿器66内の乾燥雰
囲気内で取り出す。The coagulation/pulverization container 2 sufficiently cooled by the cooling device 46 is carried into the dehumidifier 66, where the on-off valve 5 in the pressure equalization line 56 is removed.
7 or open the on-off valve 52 in the pressurizing line to solidify and
When the pressure inside the crushing chamber 50 is lowered to atmospheric pressure, large bubbles in the solidified aerated confectionery solid burst and the bottom cover 49 is then opened to open the product outlet 48 of the container body 47. , the aerated confectionery grains are taken out in a dry atmosphere within a dehumidifier 66.
空になった凝固・粉砕容器2は製品取り出し口48を蓋
49で閉塞密閉したのち気泡混入容器10T側に搬送さ
れ、菓子液導入路3.加圧ライン、均圧ライフ56のそ
れぞれを接続し、気泡混入容器1内の気泡混入菓子液を
凝固・粉砕容器2に移送し、上述の工程を繰返す。The empty coagulation/grinding container 2 is conveyed to the air bubble mixing container 10T side after the product outlet 48 is closed and sealed with a lid 49, and then passed through the confectionery liquid introduction path 3. The pressure line and the pressure equalization life 56 are each connected, and the aerated confectionery liquid in the aerated container 1 is transferred to the coagulation/pulverization container 2, and the above-mentioned steps are repeated.
なp、本発明方法では一個の気泡混入容器1に対して複
数個の凝固・粉砕容器2を用意し、この凝固・粉砕容器
2を順次使用することにより、気泡混入容器1内での気
泡混入作業を連続的に行うことができる。In the method of the present invention, a plurality of coagulation/pulverization containers 2 are prepared for one bubble-containing container 1, and the coagulation/pulverization containers 2 are sequentially used to prevent air bubbles from being mixed in the bubble-containing container 1. Work can be done continuously.
また、第7図に示すように複数個の凝固・粉砕容器2を
気泡混入容器2のT側に2個並置し、菓子液導入路3中
に分流器39を配置してpくと、一方の凝固・粉砕容器
2を接離操作している間に他方の凝固・粉砕容器2へ気
泡混入菓子液を注入することができ、作業ロスを少なく
することができる。In addition, as shown in FIG. 7, if a plurality of coagulation/pulverization containers 2 are placed side by side on the T side of the bubble mixing container 2, and a flow divider 39 is placed in the confectionery liquid introduction path 3, one side While one coagulation/pulverization container 2 is being brought into contact with and separated from the other, the aerated confectionery liquid can be injected into the other coagulation/pulverization container 2, thereby reducing work loss.
以上詳述したように、本発明方法によれば気泡混入菓子
液を収容した凝固・粉砕容器を気泡混入容器から切離し
て冷却装置に搬送し、ここで気泡混入菓子液を冷却凝固
させるようにしであるので、凝固・粉砕容器を強力に効
率良く冷却することができ、気泡入り菓子液の冷却・凝
固時間を大幅に短縮することができる。As detailed above, according to the method of the present invention, the coagulation/pulverization container containing the aerated confectionery liquid is separated from the aerated container and conveyed to a cooling device, where the aerated confectionery liquid is cooled and solidified. Therefore, the coagulation/pulverization container can be powerfully and efficiently cooled, and the cooling/solidification time of the aerated confectionery liquid can be significantly shortened.
しかも、一つの気泡混入容器に対して凝固・粉砕容器を
複数個用意し、凝固・粉砕容器を順次取替えて使用する
ことにより、凝固・粉砕容器内で気泡混入菓子液が冷却
・凝固するのに要する時間を待つ必要なく、気泡混入容
器を連続運転させることができる。In addition, by preparing multiple coagulation/pulverization containers for one air-containing container and sequentially replacing the coagulation/crushing containers, the air-filled confectionery liquid can be cooled and solidified in the coagulation/pulverization container. The bubble mixing container can be operated continuously without having to wait for a certain amount of time.
従って稼動効率を高めることができる。Therefore, operating efficiency can be improved.
そのうえ、凝固・粉砕容器からの製品の取出しを取り出
し条件の良い場所で行うことができ、製品取出し時に気
泡入り菓子粒が衝撃や吸湿などで破損して商品価値を損
うことを、簡単に防げる。In addition, the product can be removed from the coagulation/grinding container in a place with good removal conditions, and it is easy to prevent the aerated confectionery grains from being damaged by impact or moisture absorption when the product is removed, thereby reducing the product value. .
また、本発明の凝固・粉砕容器によれば、凝固・粉砕容
器内に冷却筒を位置させであるので、気泡混入菓子液を
容器本体と冷却筒とで内外両面から冷却することができ
るので、菓子液を短時間で急速に強力に冷却・凝固させ
ることができる。Further, according to the coagulation/pulverization container of the present invention, since the cooling cylinder is located inside the coagulation/pulverization container, the aerated confectionery liquid can be cooled from both the inside and outside by the container body and the cooling cylinder. Confectionery liquid can be rapidly and powerfully cooled and solidified in a short period of time.
そのうえ、冷却筒を凝固・粉砕容器の製品取出し口を閉
塞する蓋の内面に固着した構成になっているので、製品
取出し口を開放して製品を取り出す際、冷却筒が蓋とと
もに凝固・粉砕容器から抜き取られるので、製品は冷却
筒に付着して取り出されるか、冷却筒内に残置されたと
しても冷却筒が抜は出したあとに形成される空間に崩れ
出し易くなっているかするので、容器外に容易に取り出
すことができる。In addition, the cooling cylinder is fixed to the inner surface of the lid that closes the product outlet of the coagulation/grinding container, so when the product outlet is opened and the product is taken out, the cooling cylinder is attached to the lid of the coagulation/grinding container. Since the product is removed from the cooling cylinder, it may stick to the cooling cylinder and be taken out, or even if it is left inside the cooling cylinder, it may easily collapse into the space formed after the cooling cylinder is removed. It can be easily taken out.
また、凝固・粉砕容器は障害物のない空洞の状態になる
ので、製品を簡単VC@れいに取出すことができ・、歩
留りが高く経済的であるうえ、その取出し作業能率も高
い。In addition, since the coagulation/grinding container is in a hollow state with no obstructions, the product can be easily removed via VC@clean, resulting in high yield and economical efficiency.
図面は本発明方法の実施に使用する装置の一例を示し、
第1図は製造装置の正面図、第2図は気泡混入容器の要
部縦断面図、第3図は凝固・粉砕容器の縦断面図、第4
図は第3図IV−IV線断面図、第5図は作業工程の−
Rc−示す概念図、第6図は冷却方法の一例を示す概略
縦断正面図、第7図は別の実施態様を示す第1図相当図
である。
1・・・・・・気泡混入容器、2・・・・・・凝固・粉
砕容器、21・・・・・・混入器、37・・・・・・菓
子液流出口、38・・・・・・菓子液流入口、41・4
2・・・・・・仕切弁、46・・・・・・冷却装置、4
7・・・・・・凝固・粉砕容器本体、48・・・・・・
製品取出し口、49・・・・・・底蓋、51・・・・・
・ガス出入口、52・・・・・・開閉弁、61・・・・
・・フィン、62・・・・・・冷却筒、66・・曲製品
取出し室(除湿室)。The drawing shows an example of the apparatus used to carry out the method of the invention,
Figure 1 is a front view of the manufacturing equipment, Figure 2 is a vertical cross-sectional view of the main part of the bubble-containing container, Figure 3 is a vertical cross-sectional view of the coagulation/pulverization container, and Figure 4 is a vertical cross-sectional view of the coagulation/pulverization container.
The figure is a sectional view taken along the line IV-IV in Figure 3, and Figure 5 is a sectional view of the work process.
6 is a schematic longitudinal sectional front view showing an example of a cooling method, and FIG. 7 is a view corresponding to FIG. 1 showing another embodiment. 1... Bubbles mixing container, 2... Coagulation/grinding container, 21... Mixer, 37... Confectionery liquid outlet, 38...・・Confectionery liquid inlet, 41.4
2...Gate valve, 46...Cooling device, 4
7... Coagulation/grinding container body, 48...
Product outlet, 49...Bottom cover, 51...
・Gas inlet/outlet, 52... Opening/closing valve, 61...
... Fin, 62 ... Cooling cylinder, 66 ... Curved product removal chamber (dehumidification chamber).
Claims (1)
菓子粒の製造方法。 (イ)密閉した気泡混入容器1に加熱溶融した菓子原液
と圧力ガスとを注入し、気泡混入容器1内に配備した混
入器21で圧力ガスを菓子原液に気泡状に混入して圧力
気泡入り菓子液を造り、(ロ)圧力気泡入り菓子液を気
泡混入容器1から密閉した菓子液凝固・粉砕容器2VC
加圧下で移送し、 ←う この凝固・粉砕容器2を気泡混入容器1から切離
し、凝固・粉砕容器2を冷却装置46に搬送し、冷却装
置46で圧力気泡入り菓子液を凝固・粉砕容器2内で冷
却凝固させて圧力気泡入り菓子固体に造り変え、 に)冷却後の凝固・粉砕容器2を冷却装置46から製品
取出し室66に移送し、ここで凝固・粉砕容器2内から
ガス圧を抜いて、圧力気泡入り菓子固体を破裂粉砕させ
て、圧力気泡入り菓子粒を造り、しかるのち凝固・粉砕
容器2を開放。 して圧力気泡入り菓子粒を製品として凝固・粉砕容器2
から製品受取り容器に取出し、 (ホ)空になった凝固・粉砕容器2を気泡混入容器1に
接続し、 (へ)気泡混入容器1は上記工程(イ)反量←)を繰返
すとともに、凝固・粉砕容器2はそれに対応して上記工
程(o)反量(ホ)を繰返す。 2、特許請求の範囲第1項に記載した圧力気泡入り菓子
粒の製造方法KL−いて、工程←→の冷却装置46が水
槽を有し、この水槽内の水に凝固・粉砕容器2を浸漬し
て冷却するもの、 3 特許請求の範囲第1項に記載した圧力気泡入り菓子
粒の製造方法KJ、−いて、■程←→の冷封装置46が
シャワーを有し、シャワーからの噴水で凝固・粉砕容器
2を冷却するもの、 4 特許請求の範囲第1項・第2項または第3項に記載
した圧力気泡入り菓子粒の製造方法KL−いて、工程(
ロ)の凝固・粉砕容器2が気泡混入容器1の下側に配置
され、気泡混入容器1の底部に開口させた圧力気泡入り
菓子液の流出口37と凝固・粉砕容器2の上部に開口さ
せた菓子液流入口38とを2個の仕切弁41.42を介
して接続し、この接続な両弁41.42間で分離できる
ようにしたもの、 5 特許請求の範囲第1項、第2項、第3項または第4
項に記載した圧力気泡入り菓子粒の製造方法において、
一個の気泡混入容器1に対して複数個の凝固・粉砕容器
2を用意し、一個の気泡混入容器1に対して複数個の凝
固・粉砕容器2を順次取替えて使用するようにしたもの
、 6 特許請求の範囲第1項、第2項、第3項、第4項ま
たは第5項に記載した圧力気泡入り菓子粒の製造方法に
釦いて、気泡混入容器1の下側に凝固・粉砕容器2を2
個並置し、気泡混入容器1の底部に開口させた圧力気泡
入り菓子液の流出口37と各凝固・粉砕容器2の上部に
開口させた菓子液流入口38とを分岐導入路3を介して
接続したもの、 7 特許請求の範囲第1項、第2項、第3項、第4項、
第5項または第6項に記載した圧力気泡入り菓子粒の製
造方法にかいて、凝固・粉砕容器2の底面を開放して製
品取出し口48にし、製品取出し口48を底蓋49で開
閉し、凝固・粉砕容器2の上部に圧力ガス出入口51を
開口し、該圧力ガス出入口51を開閉弁52で開閉する
ようにしたもの、 8 特許請求の範囲第1項、第2項、第3項、第4項、
第5項、第6項または第7項に記載した圧力気泡入り菓
子粒の製造方法において、凝固・粉砕容器2内から製品
取出しを、除湿室66内で行うようにしたもの、 9 凝固・粉砕容器2の容器本体47に製品取出し口4
8を形成し、製品取出し口48を蓋49で開閉可能に閉
塞し、容器本体47内に突入する冷却筒62を蓋49に
固定し、冷却筒62内に冷却水を通せるように形成して
、容器本体47内を容器内外から冷却可能に構成し、容
器本体47から蓋49を取外して冷却筒62を容器本体
47外に抜出した状態では、容器本本47内で製造され
た圧力気泡入り菓子の固体が、冷却筒62表面に付着す
るか、容器本体内47の冷却筒抜去空間に崩れ出すかし
て外部に取出されるように構成したことを特徴とする圧
力気泡入り菓子粒の製造に使用する圧力気泡入り菓子液
凝固・粉砕容器、101特許請求の範囲第9項に記載し
た圧力気泡入り菓子液凝固・粉砕容器にむいて、容器本
体47を縦筒状に形成し、その上端面を閉じ切るととも
に、下端面を開放して製品取出し口48としたもの、 11 特許請求の範囲第9項または第10項に記載し
た圧力気泡入り菓子液凝固・粉砕容器に釦いて、冷却筒
62の外周面からフィン61を放射状に突設したもの、 12、特許請求の範囲第11項に記載した圧力気泡入り
菓子液凝固・粉砕容器において、フィン61の一端を蓋
49に固着して、フィン61で補強リブを兼ねさせたも
の。[Scope of Claims] 1. A method for producing pressure-bubbled confectionery grains, which includes the following steps: (b) Inject the heated and melted confectionery stock solution and pressure gas into the sealed air-mixing container 1, and mix the pressure gas into the confectionery stock solution in the form of bubbles using the mixer 21 installed inside the bubble-mixing container 1 to create pressure bubbles. A confectionery liquid coagulation/pulverization container 2VC in which a confectionery liquid is made and (b) a confectionery liquid with pressure bubbles is sealed from the air bubble mixing container 1.
The coagulation/pulverization container 2 is separated from the bubble-containing container 1, and the coagulation/pulverization container 2 is transferred to the cooling device 46, where the confectionery liquid containing pressure bubbles is coagulated and crushed into the confectionery container 2. 2) The solidified/pulverized container 2 after cooling is transferred from the cooling device 46 to the product removal chamber 66, where the gas pressure is released from inside the solidified/pulverized container 2. The solid confectionery containing pressure bubbles is ruptured and crushed to produce confectionery grains containing pressure bubbles, and then the coagulation and crushing container 2 is opened. Container 2 for coagulating and crushing confectionery grains containing pressure bubbles as a product
(e) Connect the empty coagulation/pulverization container 2 to the air bubble mixing container 1, (f) Repeat the above step (a) counter amount ←) for the air bubble mixing container 1, and solidify it. - The grinding container 2 repeats the above steps (o) and (e) in response. 2. Method KL for producing pressure-bubbled confectionery grains according to claim 1, wherein the cooling device 46 in step ←→ has a water tank, and the coagulation/pulverization container 2 is immersed in water in the water tank. 3. In the method for producing confectionery grains containing pressure bubbles KJ as set forth in claim 1, the cooling device 46 of step ←→ has a shower, and the water fountain from the shower is used to cool the confectionery grains. A device for cooling the coagulation/pulverization container 2, 4. A method for producing pressure-bubbled confectionery grains KL as set forth in Claims 1, 2, or 3.
The coagulation/pulverization container 2 of (b) is arranged below the aerated container 1, and has an outlet 37 for the pressure aerated confectionery liquid opened at the bottom of the aerated container 1 and an opening at the top of the coagulation/crushing container 2. 5. Claims 1 and 2 are connected to the confectionery liquid inlet 38 via two gate valves 41 and 42, and can be separated between the two connected valves 41 and 42. Section, Section 3 or Section 4
In the method for manufacturing confectionery grains containing pressure bubbles described in Section 1,
A plurality of coagulation/pulverization containers 2 are prepared for one bubble mixing container 1, and the plurality of coagulation/pulverization containers 2 are sequentially replaced and used for one bubble mixing container 1, 6 In accordance with the method for producing pressure-bubbled confectionery grains as set forth in claim 1, 2, 3, 4, or 5, a coagulation/pulverization container is provided below the bubble-containing container 1. 2 to 2
The pressure bubbled confectionery liquid outlet 37 opened at the bottom of the bubble mixing container 1 and the confectionery liquid inlet 38 opened at the top of each coagulation/pulverization container 2 were connected to each other via the branch introduction path 3. 7 Claims 1, 2, 3, 4,
In the method for producing pressure-bubbled confectionery grains described in item 5 or 6, the bottom of the coagulation/grinding container 2 is opened to form a product outlet 48, and the product outlet 48 is opened and closed with a bottom lid 49. , a pressure gas inlet/outlet 51 is opened in the upper part of the coagulation/pulverization container 2, and the pressure gas inlet/outlet 51 is opened/closed by an on-off valve 52; 8. Claims 1, 2, and 3. , Section 4,
9. A method for producing pressure-bubbled confectionery grains as described in item 5, item 6, or item 7, in which the product is removed from the coagulation/pulverization container 2 in the dehumidification chamber 66; 9. Coagulation/grinding A product outlet 4 is provided in the container body 47 of the container 2.
8, the product outlet 48 is openably and closably closed with a lid 49, a cooling cylinder 62 protruding into the container body 47 is fixed to the lid 49, and the cooling cylinder 62 is formed so as to allow cooling water to pass therethrough. The inside of the container body 47 can be cooled from inside and outside of the container, and when the lid 49 is removed from the container body 47 and the cooling tube 62 is pulled out of the container body 47, the pressure bubbles produced inside the container body 47 can be cooled. Production of confectionery grains containing pressure bubbles, characterized in that the solids of the confectionery are taken out to the outside by adhering to the surface of the cooling tube 62 or collapsing into the cooling tube extraction space 47 inside the container body. For the confectionery liquid coagulation and crushing container containing pressure bubbles used for confectionery liquid coagulation and crushing, the container main body 47 is formed into a vertical cylinder shape, and the container body 47 is formed into a vertical cylinder shape, and The end face is completely closed and the lower end face is opened to form a product outlet 48. 11. A cooling cylinder which is attached to the pressurized bubble confectionery liquid coagulation/grinding container described in claim 9 or 10. 12. In the pressure bubble confectionery liquid coagulation and crushing container described in claim 11, one end of the fin 61 is fixed to the lid 49, Fin 61 doubles as a reinforcing rib.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55021992A JPS5826942B2 (en) | 1980-02-22 | 1980-02-22 | Method for producing pressure-bubbled confectionery granules and pressure-bubbled confectionery liquid coagulation/grinding container used therein |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55021992A JPS5826942B2 (en) | 1980-02-22 | 1980-02-22 | Method for producing pressure-bubbled confectionery granules and pressure-bubbled confectionery liquid coagulation/grinding container used therein |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56117755A JPS56117755A (en) | 1981-09-16 |
JPS5826942B2 true JPS5826942B2 (en) | 1983-06-06 |
Family
ID=12070512
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55021992A Expired JPS5826942B2 (en) | 1980-02-22 | 1980-02-22 | Method for producing pressure-bubbled confectionery granules and pressure-bubbled confectionery liquid coagulation/grinding container used therein |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5826942B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2771849B2 (en) * | 1989-06-23 | 1998-07-02 | エス・ティ・エス株式会社 | Cooling system using external surface cooler for avionics |
JPH0775833B2 (en) * | 1991-03-18 | 1995-08-16 | 日本炭酸株式会社 | Dry ice cutting equipment |
JP4642051B2 (en) * | 2007-09-06 | 2011-03-02 | 日清製粉株式会社 | Manufacturing method of donut-like food |
-
1980
- 1980-02-22 JP JP55021992A patent/JPS5826942B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS56117755A (en) | 1981-09-16 |
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