JPS6349040A - Production of low-density fat and oil cake - Google Patents

Production of low-density fat and oil cake

Info

Publication number
JPS6349040A
JPS6349040A JP61192844A JP19284486A JPS6349040A JP S6349040 A JPS6349040 A JP S6349040A JP 61192844 A JP61192844 A JP 61192844A JP 19284486 A JP19284486 A JP 19284486A JP S6349040 A JPS6349040 A JP S6349040A
Authority
JP
Japan
Prior art keywords
dough
oil
based confectionery
low
chocolate
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
JP61192844A
Other languages
Japanese (ja)
Other versions
JPH0338820B2 (en
Inventor
Iwao Hachiya
巌 蜂屋
Tetsuo Koyano
哲夫 古谷野
Norio Kamiyama
上山 矩生
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.)
Meiji Seika Kaisha Ltd
Original Assignee
Meiji Seika Kaisha Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Meiji Seika Kaisha Ltd filed Critical Meiji Seika Kaisha Ltd
Priority to JP61192844A priority Critical patent/JPS6349040A/en
Publication of JPS6349040A publication Critical patent/JPS6349040A/en
Publication of JPH0338820B2 publication Critical patent/JPH0338820B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Confectionery (AREA)

Abstract

PURPOSE:To produce a low-density fat and oil cake having uniformly dispersed fine foams, good melting in the mouth, extreme fineness and improved appearance, by cooling tempered type fat and oil dough, introducing an inert gas to the dough under pressure and stirring the dough forcedly. CONSTITUTION:Ordinary tempered type fat and oil cake dough optionally mixed with about 0.5wt% emulsifying agent is melted and the temperature of the dough is reduced to raise the viscosity to about 300,000-500,000cps. Then the dough is sent to a continuous pressurizing and foaming mixer with a cooling jacket such as OHKS mixer, simultaneously 1.2-2.5 times as much an inert gas in a normal condition as the cake dough by volume is uniformly dispersed into the dough while cooling the dough and the gas is discharged to normal pressure to give low-density fat and oil cake dough uniformly containing foams with <=about 0.3mm diameter and 0.6-0.8 specific gravity, which is formed by a conventional procedure, cooled and solidified.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明はチョコレート等の油脂性菓子に微小な気泡を均
一に分散させて比重を0.60〜0.80程度とした軟
らかい噛み心地と滑らかな舌ざわりを有し、口溶けが良
好で、しかもきめの細かい外観のすぐれた低密度油脂性
菓子を製造する方法に関する。
Detailed Description of the Invention [Industrial Field of Application] The present invention uniformly disperses minute air bubbles in oil-based confectionery such as chocolate to give it a soft chewing feel and smooth texture with a specific gravity of about 0.60 to 0.80. This invention relates to a method for producing a low-density oil-based confectionery that has a pleasant texture, melts well in the mouth, and has a fine texture and appearance.

[従来の技術] 従来、油脂性菓子生地に気泡を含有させた軽い食感を有
する低密度油脂性菓子の製造方法としては、(1)常圧
でホイップし、生地中に気泡を抱き込ませる方法(特開
昭60−58037号) 、 (2)減圧下で生地中の
気泡を膨化させて多孔質化する方法(特公昭60−35
093号) 、 (3)高圧下で生地中にガスを溶解及
び/又は分散させた後、常圧に戻して発泡状の生地を製
造する方法(特公昭57−21293号)等の諸方法が
知られている。(1)の方法は。
[Prior Art] Conventionally, methods for producing low-density oil-based confectionery with a light texture by incorporating air bubbles into oil-based confectionery dough include (1) whipping at normal pressure to incorporate air bubbles into the dough; method (Japanese Patent Publication No. 60-58037), (2) Method of expanding air bubbles in the dough under reduced pressure to make it porous (Japanese Patent Publication No. 60-35
093), (3) A method in which gas is dissolved and/or dispersed in the dough under high pressure and then returned to normal pressure to produce foamed dough (Japanese Patent Publication No. 57-21293). Are known. What is method (1)?

通常の調温タイプのチョコレートに液状脂を含む油脂を
20〜25%程度添加配合し、全体の油脂含量を60%
程度の高含量にしてこれをボテーターまたはフンビネー
ター等により急冷混捏してチョコレートに起泡性を付ケ
し、続いてオーバーミキサーによりホイップして50〜
100%の高オーバーランのチョコレート(比重換算で
0.5〜0.7)を製造するものである。また、(2)
の方法は、予め気泡を包含させた油脂性菓子生地を成形
型内に流し込み錘を載せた蓋等で該成形型内の生地を加
圧しながら減圧下に置く事により生地の表面、内部及び
底部の気泡を均質に膨化した多孔質の油脂性菓子を製造
するものである。さらに、(3)の方法は、密閉容器中
で液状のチョコレートに高圧ガスを溶解及び/又は分散
せしめ、次いで急激に圧力を解く1ハにより生地中の溶
解ガスの気体化及び/又は分散ガスの体膨張により発泡
状のチョコレート生地を製造するものである。
Approximately 20 to 25% of fats and oils, including liquid fats, are added to regular temperature-controlled chocolate to bring the total fat content to 60%.
This is then rapidly cooled and kneaded using a votator or humbinator to give the chocolate a foaming property, and then whipped using an over mixer to give it a 50~
Chocolate with a high overrun of 100% (0.5 to 0.7 in terms of specific gravity) is produced. Also, (2)
This method involves pouring oil-based confectionery dough into which air bubbles have been pre-filled into a mold, pressurizing the dough inside the mold with a lid equipped with a weight, etc., and placing it under reduced pressure. This method produces porous oil-based confectionery with uniformly expanded air bubbles. Furthermore, method (3) involves dissolving and/or dispersing high-pressure gas in liquid chocolate in a closed container, and then rapidly releasing the pressure to vaporize the dissolved gas in the dough and/or to disperse the dispersed gas. This method produces foamy chocolate dough by expanding the body.

[発明が解決しようとする問題点] E記(1)の方法を記載した特開昭80−58037号
の方法によれば、比較的簡便にバタークリーム様に滑ら
かな食感を有する高ホイップの調温タイプチョコレート
を製造することが出来るが、この公報が開示している様
に、急冷混捏処理により優れた起泡性を付ゲすることが
出来るのは1通常の調温タイプのチョコレートに起泡特
性の向ヒを意図して液状脂を含む添加油脂を20〜25
%も多量に添加してカカオ脂及び/又はハードバターの
シャープな溶解特性を改質した場合に限られるのである
。それ故、多量の添加油脂によりカカオマスや粉乳等の
呈味成分の含量が通常のチョコレートに比し低く、風味
の乏しい低密度チョコレートとなる。そしてカカオ脂及
び/又はカカオ脂と同等の溶解特性を有するハードバタ
ーを主体油脂とする通常の調温タイプのチョコレートを
使用した場合にはこの方法によりバタークリーム様のき
めの細かさと軽い食感とを有する低密度チョコレートを
製造することは出来ない。さらに、ホイップした生地は
空気を多量に生地中に含有させる事にfiす、空気と生
地との接触面積の飛躍的な増加によりチョコレート成分
、特に油脂の酸化が促進され、風味劣化をもたらすが、
この対策について全く明示されていない。
[Problems to be Solved by the Invention] According to the method of JP-A No. 80-58037 which describes the method of item E (1), highly whipped cream having a buttercream-like smooth texture can be produced relatively easily. Temperature-controlled chocolate can be produced, but as disclosed in this publication, only one type of chocolate that can be given excellent foaming properties by rapid cooling and kneading is produced from ordinary temperature-controlled chocolate. 20 to 25% of added oil containing liquid fat was added to improve the foaming properties.
% is added in large quantities to modify the sharp dissolution characteristics of cocoa butter and/or hard butter. Therefore, due to the large amount of added fat and oil, the content of flavor components such as cacao mass and powdered milk is lower than that of ordinary chocolate, resulting in low-density chocolate with poor flavor. When using regular temperature-controlled chocolate whose main fat is cacao butter and/or hard butter that has the same melting properties as cacao fat, this method produces buttercream-like fine texture and light texture. It is not possible to produce low-density chocolate with Furthermore, whipped dough contains a large amount of air, which dramatically increases the contact area between the air and the dough, which accelerates the oxidation of chocolate ingredients, especially fats and oils, resulting in flavor deterioration.
This measure is not specified at all.

−・方、減圧処理により多孔質のチョコレートを製造す
る(2)の方法を示している特公昭80−35093号
によれば、通常の調温タイプのチョコレートでも低密度
チョコの製造が可使であるが、調温処理したチョコレー
トを減圧した型中で膨化させた後、常圧に戻した時にチ
ョコレートの多孔質骨格が崩れない程度迄減圧状態を保
持したままで該チョコレートを冷却固化させねばならず
、装置が複雑で大型化するという欠点がある。しかも、
チョコレート中の気泡の減圧下での膨化時に膨化率は減
圧程度とは比例せず、チョコレートの粘性抵抗を越える
程度の減圧度になると急激に膨化が起こるために、気泡
の大きさが大きくならざるを得す0.8〜1.5mmも
の孔が分散したハニカム状構造になってしまう、それ故
、製品チョコレートの割面は穴だらけの状態を呈する和
となり、舌ざわりが粗くカリカリした噛み心地のものに
なってしまう欠点がある。さらに、この孔内は防圧とな
っているために、製品を常圧丁に保持した時に空気がチ
ョコレートの骨格を透過して孔内に入ってしまい、油脂
等の成分の酸化変敗がキくなり風味劣化をもたらし易い
、また、L記(3)の方法について開示している特公昭
57−21293号は泡入キセンディー生地、マシマロ
生地等の泡入菓子の製造において使用されている通常の
方法をチョコレートに適用したのにすぎず、他の菓子生
地とは異なるチョコレートの特異的な物性9品質を何ら
配慮していない安直な方法と言わざるを得ない。すなわ
ち、この方法によれば、まずチョコレートの液状状態を
保持する為、少なくとも35℃以Eの温水で全r程を保
温して行なっている。しかし、通常の調温型のチョコレ
ートは、品温を−E(28〜27℃まで下げ、しかる後
30°C程度までEげて安定型の油脂結晶結晶核を形成
させる調温処理を行わないと、冷却固化時にチョコレー
ト製品中に7アツトブルームと称される油脂の粗大結晶
が生じ表面が灰白色となり、組織も粗くなってチョコレ
ート本来の色調、舌ざわりを全く失い、商品価値がなく
なる。しかるに、チョコレート中の結晶の結晶核の融点
は精々31℃程度であり、35℃にもなれば油脂は完全
に溶解している状態となり、これをそのまま冷却固化し
た時にはL記したプルーム現象が起こり、品質的に全く
劣ったものとなる。また、粘度についての記載がないの
で明確でないが、通常の液状チョコレートは粘度が20
,000〜50,000cpsで流動性に富んでおり、
この様なチョコレート生地では生地中にガスを均一に分
散させても分散のための攪拌を止めた瞬間にガス気泡は
生地中を浮上移動し、気泡同志が集合して、大きな気泡
となり生地から抜は出してしまい、発泡状のチョコレー
ト生地が得られない。このことは、後記する様に、通常
のチョコレート生地をオーバーミキサー等でホイップし
ても好適な低密度のチョコレートが得られない2バによ
っても明らかであり、均一分散したガス気泡が生地中で
移動しない様保持するには生地がほとんど流動性を消失
した状態にある300,000〜500,000cps
程度の粘度を必要とし、チョコレートの流動性を利用す
る通常の成形工程では全く用いられる事のない極端に増
粘処理した生地ではじめて可能となるものである0本件
公報に記載されている様に、ベルトコンベアl−の発泡
状チョコレート生地に振動をかえると、気泡のセル壁が
破壊して個々の気泡が合体して大きくなるという気泡移
動の自由な低粘度の生地によっては、後記する様な本発
明による高品質な低密度油脂性菓子の製造は全く不可能
である。
- On the other hand, according to Japanese Patent Publication No. 80-35093, which describes method (2) of producing porous chocolate by vacuum treatment, it is possible to produce low-density chocolate even with regular temperature-controlled chocolate. However, after temperature-controlled chocolate is expanded in a mold under reduced pressure, the chocolate must be cooled and solidified while maintaining the reduced pressure to such an extent that the porous framework of the chocolate does not collapse when the pressure is returned to normal. First, it has the disadvantage that the device is complicated and large. Moreover,
When air bubbles in chocolate expand under reduced pressure, the expansion rate is not proportional to the degree of pressure reduction, and when the degree of pressure reduction exceeds the viscous resistance of chocolate, expansion occurs rapidly, so the size of the bubbles does not increase. This results in a honeycomb-like structure with dispersed pores of 0.8 to 1.5 mm, which results in the cut surface of the finished chocolate being full of holes, giving it a rough texture and a crunchy texture. There is a drawback that it becomes Furthermore, since the inside of this hole is pressure-proof, when the product is held under normal pressure, air passes through the chocolate skeleton and enters the hole, preventing oxidation and deterioration of ingredients such as oil and fat. In addition, Japanese Patent Publication No. 57-21293, which discloses the method described in L. It must be said that this method is simply an application of the method to chocolate, and is a simple method that does not take into account the unique physical properties of chocolate that differ from other confectionery doughs. That is, according to this method, in order to maintain the liquid state of the chocolate, the whole chocolate is kept warm with hot water of at least 35° C. or higher. However, regular temperature-controlled chocolate does not undergo a temperature-control process in which the product temperature is lowered to -E (28 to 27 degrees Celsius) and then raised to about 30 degrees Celsius to form stable fat crystal nuclei. When the chocolate product cools and solidifies, coarse crystals of oil and fat called 7-at-bloom occur in the chocolate product, the surface becomes grayish white, and the texture becomes coarse, causing the chocolate to completely lose its original color and texture, and lose its commercial value.However, chocolate The melting point of the crystal nucleus of the crystals inside is about 31℃ at most, and if the temperature reaches 35℃, the fats and oils will be completely dissolved. It is completely inferior to the viscosity.Also, it is not clear because there is no mention of viscosity, but normal liquid chocolate has a viscosity of 20%.
,000 to 50,000cps and has high fluidity.
In this kind of chocolate dough, even if the gas is uniformly dispersed in the dough, the moment you stop stirring for dispersion, the gas bubbles float up and move through the dough, and the gas bubbles gather together to form large bubbles that are pulled out of the dough. The foam will come out and you won't be able to get a foamy chocolate dough. This is also clear from the case of No. 2, where a suitable low-density chocolate cannot be obtained even if normal chocolate dough is whipped with an over mixer, etc., as described later, and uniformly dispersed gas bubbles move in the dough. 300,000 to 500,000 cps when the dough has almost lost its fluidity to maintain the fluidity.
This is possible only with extremely thickened dough, which requires a certain degree of viscosity and is never used in the normal molding process that utilizes the fluidity of chocolate. When the foamed chocolate dough on the belt conveyor l- is vibrated, the cell walls of the bubbles break down and the individual bubbles coalesce and become larger. It is simply not possible to produce high-quality low-density oil-based confections according to the invention.

[問題点を解決するためのf段] 本発明者等はヒ記した従来技術の間欠点をなくし、シャ
ープな溶解特性を有するカカオ脂及び/又はハードパタ
ーを主体油脂とする通常のテンパー型油脂性菓子につい
てこれを柔い噛み心地で滑らかな舌ざわりとシャープな
口溶けを有し、きめの細かい外観のすぐれた低密度油脂
性菓子を効率的に製造する方法について検討した結果、
テンパー型油脂性生地をテンパリング処理せず、単に冷
却のみで適宜な粘性を持つように調製し、これに不活性
ガスを圧入して強制攪拌する事でガスを生地中に微細均
一に分散させると、比重が0.8〜0.8程度でバター
クリーム状の組織と食感とを有し、ファツトブルームが
なくて保存性の良い低密度油脂性菓子を容易に連続製造
し得る事を見出し、さらに検討を重ねて本発明を完成す
るに到った。
[Step F for solving the problems] The present inventors have solved the drawbacks of the conventional techniques described above, and have developed a conventional tempering type oil and fat mainly composed of cacao butter and/or hard putter, which have sharp solubility characteristics. As a result of studying how to efficiently produce low-density oil-based confectionery with a soft texture, smooth texture, and sharp melt-in-the-mouth texture, and a fine-grained appearance, we found that:
Temper-type oil-based dough is prepared by simply cooling it without tempering to give it an appropriate viscosity, and by pressurizing inert gas and forcibly stirring, the gas is dispersed finely and uniformly into the dough. It was discovered that a low-density oil-based confectionery with a specific gravity of about 0.8 to 0.8, a buttercream-like structure and texture, no fat bloom, and good shelf life could be easily and continuously manufactured. After further study, the present invention was completed.

以ド、本発明を代表的実施例により説明する。The present invention will now be described by way of representative examples.

本発明では通常の方法で製造したカカオ脂及び/又はカ
カオ脂と同等の溶解特性を有するハードパターを主体構
成油脂とするテンパー型のチョコレート、ホワイトチョ
コレート、カラーチョコレート等の油脂性菓を生地を用
いる。まず、溶融した該生地をモイノポンプ等の定1龜
式ポンプでボテーター、コンビネータ−等の掻取型の熱
交換機中に送り、生地の定温化を計る。温度は35〜4
0°C付近の適宜な温度を設定し、品温のバラツキを設
定温度の±0.5℃以内とする。そして次に、これをそ
のまま冷却用のジャケット付ビン型攪拌熱交換機に送る
。そして油脂性菓子生地の品温を低下させ、粘度を30
0.000〜500.000cps程度まで上昇させる
。次いで、該生地をそのままジャケット部に冷媒が循環
して冷却しているオークス・ミキサー等の連続加圧泡立
てミキサーに送入し、同時にガスを適宜量注入して生地
の品温を−1−げない様冷却しつつ、ガスを生地中に均
一に分散させ、しかる後排出する0通常のテンパー型油
脂性菓子生地は溶融時に比重1.20〜1.25で30
,000〜70.000cps程度の粘度を有している
が、この程度の粘度では生地を攪拌して空気又はガスを
混合した場合、生地中での空気の浮力が生地の粘性抵抗
よりはるかに大きい為、はとんどのガスが攪拌の停止と
共に抜けてしまい前記した様な高品質の低密度油脂性菓
子は製造出来ない。
In the present invention, the dough is used to make oil-based confectionery such as tempered chocolate, white chocolate, and colored chocolate, whose main constituent fat is cacao butter and/or hard putter having the same dissolution characteristics as cacao butter, produced by a conventional method. . First, the molten dough is sent to a scraping-type heat exchanger such as a votator or a combinator using a constant-pump pump such as a Moino pump, and the temperature of the dough is kept constant. Temperature is 35-4
Set an appropriate temperature around 0°C, and keep the variation in product temperature within ±0.5°C of the set temperature. Next, this is directly sent to a jacketed bottle-type stirring heat exchanger for cooling. Then, lower the temperature of the oil-based confectionery dough and reduce the viscosity to 30%.
It is increased to about 0.000 to 500.000 cps. Next, the dough is fed as it is into a continuous pressurized whisking mixer such as an Oaks mixer that is cooled by circulating a refrigerant through the jacket, and at the same time an appropriate amount of gas is injected to bring the temperature of the dough down to -1. The gas is uniformly dispersed in the dough while being cooled, and then discharged. 0 Normal tempered oil-based confectionery dough has a specific gravity of 1.20 to 1.25 when melted.
It has a viscosity of about ,000 to 70,000 cps, but at this level of viscosity, when the dough is stirred and air or gas is mixed, the buoyancy of the air in the dough is much greater than the viscous resistance of the dough. Therefore, most of the gas escapes when stirring is stopped, making it impossible to produce high-quality low-density oil-based confectionery as described above.

それ故、本発明では生地の粘度を調整して、生地中に強
制的にガスを分散させる時攪拌を停止してもガスが抜け
ない程度の高粘度にして含気させるのである。その粘度
調整にはチョコレート等の油脂性菓子生地を冷却し、油
脂の結晶化による増粘現象を利用するのであるが、これ
を連続して安定して実施するために、該生地を溶融温度
域で適宜の設定温度に対し±0.5℃以内に管理するの
が好ましい、この場合、品温のバラツキが大きいと、続
いて実施する冷却増粘工程での粘度のバラツキが大きく
なり、ガスの強制分散工程で生地内にガスを保持出来な
い程度の含気性のない低粘度の生地になったり又は生地
粘度が大きくなり過ぎて配管内の抵抗等が急激に上昇し
、生地送り用のポンプに大きい負荷がかかったり、生地
流量が極端に少くなったりして安定した製造が困難とな
る。
Therefore, in the present invention, the viscosity of the dough is adjusted so that the viscosity is high enough to prevent gas from escaping even if stirring is stopped when the gas is forcibly dispersed in the dough. To adjust the viscosity, oil-based confectionery dough such as chocolate is cooled and the thickening phenomenon caused by the crystallization of oil and fat is utilized. It is preferable to control the temperature within ±0.5℃ with respect to the appropriate set temperature. In this case, if there is a large variation in the product temperature, the viscosity in the subsequent cooling thickening process will increase, and the gas During the forced dispersion process, the dough becomes so low in viscosity that it cannot retain gas, or the dough becomes too viscous, causing a sudden increase in resistance in the piping, causing problems with the dough feeding pump. Stable production becomes difficult due to heavy loads and extremely low dough flow rates.

一5方、冷却攪拌による生地の増粘工程では、生地中の
油脂が結晶化し、生地粘度は品温及び滞留時間を必要と
する。さらに、生地粘度のと昇により攪拌抵抗も著しく
増大するので、この工程用の冷却攪拌装置としてはビン
型攪拌熱交換機が適している。L記した連続冷却攪拌工
程の採用により生地の含気性が高くなり好適である。こ
のようにして粘度り昇した生地は、そのままガス強制分
散装置である連続加圧泡立てミキサーに送入される。ガ
ス強制分散装置としては攪拌羽根の枚数が多数あり、し
かも攪拌羽根間のクリアランスが狭いオークス・ミキサ
ー等の連続加圧泡立てミキサーがガスの均質分散能がす
ぐれており好適である。そして、このミキサーによる攪
拌分散時の発熱により油脂結晶が一部溶解して生地粘度
が低下する。その結果、含気性が低下する為、連続加圧
泡立てミキサー内の圧力は8〜12kg/cm2程度に
なる。i1!続加圧泡立てミキサー内に圧入する高圧ガ
スは、1気圧、20℃の標準状態に換算してチョコレー
ト等の油脂性菓子生地量に対し、1,2〜2.5倍容量
とする。圧入するガス量が該生地量に対して少なすぎる
と、含有量の少ない硬い尚ごたえのチョコレートになる
し、一方必要以上に多すぎると、生地の含気能を越えて
分散出来ない過剰分は生地から分離して大気中に逃げる
事となり無駄である。クリーミーでソフトな食感と噛み
心地及びシャープな口溶けを有し、巨つ外観上滑らかな
きめの細かい生地とするには生地中に分散する気泡の径
が0.3■以下と非常に小さくなければならず、又生地
の比重も0.8程度以下の低密度にする必要がある。
On the other hand, in the process of thickening the dough by cooling and stirring, the fats and oils in the dough crystallize, and the viscosity of the dough requires temperature and residence time. Furthermore, as the viscosity of the dough increases, the stirring resistance increases significantly, so a bottle-type stirring heat exchanger is suitable as the cooling stirring device for this process. Adoption of the continuous cooling and stirring process described in L increases the air content of the dough, which is preferable. The dough, which has increased in viscosity in this way, is directly fed into a continuous pressurized whisking mixer, which is a forced gas dispersion device. As a forced gas dispersion device, a continuous pressurized foaming mixer such as an Oaks mixer, which has a large number of stirring blades and a narrow clearance between the stirring blades, is suitable because it has excellent ability to homogeneously disperse gas. The heat generated during stirring and dispersion by this mixer causes some of the fat and oil crystals to dissolve, reducing the viscosity of the dough. As a result, the air content decreases, and the pressure inside the continuous pressurized foaming mixer becomes approximately 8 to 12 kg/cm2. i1! The volume of the high-pressure gas injected into the continuous pressurized whisking mixer is 1.2 to 2.5 times the amount of oil-based confectionery dough such as chocolate when converted to standard conditions of 1 atmosphere and 20°C. If the amount of gas to be injected is too small relative to the amount of dough, the chocolate will have a hard and chewy texture with a low content, while if it is too much than necessary, the excess gas that cannot be dispersed will exceed the air holding capacity of the dough. It separates from the dough and escapes into the atmosphere, which is wasteful. In order to create a smooth, fine-grained dough that has a creamy, soft texture, a chewy feel, and a sharp melt-in-the-mouth texture, the diameter of the air bubbles dispersed in the dough must be extremely small, less than 0.3 cm. In addition, the specific gravity of the fabric needs to be low, about 0.8 or less.

本発明では油脂性菓子生地の粘度を調節する!バで生地
の含気性を高め、上記圧入ガス量で比重が0.6〜0.
8程度の低密度チョコレートを製造することが出来る。
In the present invention, the viscosity of oil-based confectionery dough is adjusted! The air permeability of the fabric is increased using a steamer, and the specific gravity is increased to 0.6-0.
It is possible to produce low density chocolate of about 8.

常圧で比較した時、圧入するガス量に比して生地の体積
膨化が小さいのは、生地中に高圧で分散したガス気泡は
生地が常圧に戻された時に内圧力で膨化するものの、生
地の粘度が著しく高く抵抗が大きいため、膨化が抑制さ
れ陽圧状態のままで分散する事となるのである。
When compared at normal pressure, the volume expansion of the dough is small compared to the amount of gas injected. Although gas bubbles dispersed in the dough at high pressure expand due to internal pressure when the dough is returned to normal pressure. Since the viscosity of the dough is extremely high and the resistance is large, swelling is suppressed and the dough is dispersed under positive pressure.

圧入するガスは油脂性菓子の成分、特に油脂成分の酸化
変敗な防止するため、窒素や炭酸ガス等の不活性ガスを
用いるのが良い、また、予め不活4性ガスと揮発性の香
気成分を混合して付番したガスを圧入する事も出来る。
It is best to use an inert gas such as nitrogen or carbon dioxide as the gas to be pressurized, in order to prevent oxidation and deterioration of the components of oil-based confectionery, especially the oil and fat components. It is also possible to mix the components and inject a numbered gas under pressure.

この場合、食べた時の香り立ちが非常にすぐれたものと
なる。このようにして製造した低密度油脂性菓子生地は
経時的に粘度がさらにと昇し、 800,000−1,
000,000cps程度のほとんど流動性のない生地
になる。これをそのまま冷却固化した後、ナイフ等で切
削して適宜な形状に成形するか又はブライン冷媒で冷却
した一対の刻設型付ロール間に供給して成形した後、さ
らに冷却固化して製品とする。
In this case, the flavor will be very good when eaten. The viscosity of the low-density oil-based confectionery dough produced in this way further increases over time, and the viscosity increases to 800,000-1.
The result is a dough with almost no fluidity of about 0,000,000 cps. After cooling and solidifying it as it is, it is either cut with a knife or the like and formed into an appropriate shape, or it is fed between a pair of engraved rolls cooled with brine refrigerant and molded, and then further cooled and solidified to form a product. do.

本発明ではテンパー型油脂性菓子生地を用い、しかも通
常のテンパリングを行わないにもかかわらず、製造され
た製品は長期間室温に保存してもブルーミングを全く生
じない、その理由は明確ではないが、加圧泡立て攪拌工
程中生地は冷却されると共に攪拌による発熱もある為、
ミクロの状態でテンパリングと全く同様な調温処理効果
を受けて安定な微細結晶となるものと考えられる。
Although the present invention uses tempered oil-based confectionery dough and does not undergo normal tempering, the manufactured product does not exhibit any blooming even when stored at room temperature for a long period of time.The reason for this is not clear, but During the pressurized whisking and stirring process, the dough is cooled and also generates heat due to stirring.
It is thought that stable microcrystals are formed in the microscopic state through a temperature control treatment effect similar to tempering.

一方、生地の含気性の向上を意図して適宜の乳化剤を添
加配合することも効果的である。例えば、ポリグリセリ
ン脂肪酸エステル系の乳化剤であるテトラグリセリンペ
ンタステアレートをチョコレートなどの油脂性菓子生地
に0.5%程度添加すると、含気性は該乳化剤を添加し
ない場合に比して比重で0.05〜0.IO程度小さく
、それだけ軽い食感の製品が得られるので好適である。
On the other hand, it is also effective to add and blend an appropriate emulsifier with the intention of improving the air permeability of the dough. For example, when about 0.5% of tetraglycerol pentastearate, which is a polyglycerol fatty acid ester emulsifier, is added to oil-based confectionery dough such as chocolate, the air content becomes 0.5% in specific gravity compared to when the emulsifier is not added. 05~0. This is preferable because it is about IO smaller and a product with a lighter texture can be obtained.

但し、0.5%以上添加しても含気性はさほど向トしな
いし、逆に乳化剤自身の好ましくない味が油脂性菓fに
付かされることになる。
However, adding 0.5% or more does not significantly improve the air content, and conversely, the undesirable taste of the emulsifier itself will be imparted to the oil-based confectionery f.

本発明では通常のテンパー型油脂性菓子生地と同等又は
それよりやや高い融点を有するノンテンパー型油脂性菓
了生地でも全く同様の方法でテンパー型油脂性菓子生地
の場合とほぼ同様な風味。
In the present invention, a non-tempered oil-based confectionery dough having a melting point equal to or slightly higher than that of a normal tempered oil-based confectionery dough can be used in exactly the same manner to obtain almost the same flavor as that of a tempered oil-based confectionery dough.

食感及び外観を呈する比重0.6〜0.8の低密度チョ
コレートを容易に製造出来る。尚、油脂性菓り生地の粘
度は東京計器製作所のB型粘度計を用い、+00.00
0cps以下の場合はローター#6゜4rpmで、10
0.000cps以上の場合はローター#7,4rpm
で測定した値である。
Low-density chocolate with a specific gravity of 0.6 to 0.8 that exhibits good texture and appearance can be easily produced. In addition, the viscosity of the oil-based confectionery dough was measured using a B-type viscometer manufactured by Tokyo Keiki Seisakusho.
If it is less than 0 cps, rotor #6°4 rpm, 10
If 0.000cps or more, rotor #7, 4rpm
This is the value measured at

[発明の効果] 本発明により従来の技術ではその製造が極めて困難であ
ったカカオ脂及び/又はカカオ脂と同様なシャープな溶
解特性を有するハード八ターを主要構成油脂とするテン
パー型油脂性菓子生地及び/又はカカオ脂よりやや劣る
がシャープな溶解時し、これ等を単純に冷却するだけで
生地に含気性を付ケし、さらにこれ等に不活性ガスを強
制的に分散させる簡便な装置と方法により径0.3■以
下の微小な気泡を生地中に均一に分散させた1口溶は良
好でしかもきめの細い外観のすぐれた比重0.6〜0.
8程度の低密度の油脂性菓子を極めて効率良く製造する
ことが出来る。不活性ガスを生地中に分散させている為
、この油脂性菓子は長期保存時に酸化変敗による風味劣
化がほとんど生ぜず、また付番した不活性ガスの使用時
には、喫食詩の香り立ちかさらに著しく良好な製品とす
る4Sが出来る。
[Effects of the Invention] The present invention provides a tempered oil-based confectionery whose main constituent fat is cacao butter and/or a hard fat having sharp dissolution characteristics similar to cacao butter, which was extremely difficult to produce using conventional techniques. A simple device that dissolves sharply, although slightly inferior to dough and/or cacao butter, and makes the dough air-permeable by simply cooling it, and also forcibly disperses inert gas into it. Using this method, the one-bite melt, in which minute air bubbles with a diameter of 0.3 square meters or less are uniformly dispersed in the dough, has a fine texture and an excellent specific gravity of 0.6 to 0.
Oil-based confectionery with a low density of about 8 can be produced extremely efficiently. Because inert gas is dispersed in the dough, this oil-based confectionery hardly suffers from flavor deterioration due to oxidation during long-term storage, and when using the numbered inert gas, it has an even more aromatic aroma. 4S can be achieved to make the product extremely good.

[実施例] カカオマス18.0部、砂糖38.75部、乳糖5.0
部、レシチン0.5部、アーモンド粉末1.0部。
[Example] 18.0 parts of cacao mass, 38.75 parts of sugar, 5.0 parts of lactose
part, lecithin 0.5 part, almond powder 1.0 part.

ココアバター8.1部、全脂粉乳20.0部およびテン
パー型ハードバター(融点35.0℃、商品名、メラノ
SS 200) 10.85部を配合し、常法に従い油
脂含量34.2%のテンパー型のミルクチョコレート生
地を得た。50〜55°Cで溶融して粘度が65,00
0cpsの該生地をモイノポンプによりジャケット部に
40℃の温水を循環させた掻取型攪拌熱交換機に時間当
り120kg定沿送入した。この時該生地の熱交換機出
口での品温は40℃±0.4℃であった0次に、該生地
を掻取型攪拌成熱交換機出口に接続したパイプを通して
10℃のブラインを循環したジャケット部に100〜1
20ビン型纜拌熱交換機に送入し、生地を冷却して出口
品温を26〜25.8℃とした。その時の生地の粘度は
300.000cps〜400.000cpsであった
。該生地をさらにビン型攪拌熱交換機出[1に接続した
バイブにてブラインを循環し、40rpmで攪拌したジ
ャケット部に一25℃のオークスミキサ−(C9M型連
続ケーキミキサー)に送入した。この時、圧力は攪拌部
入口で11kg/cm2 、攪拌部出口で3 kg/c
m2であった。J!jl拌部入口部入口力15kg/c
m2の窒素ガスを流量調節装置を通して標や状態で3.
2 U分の割合でJ!I続して排出した。このようにし
て得た生地は品温25.8℃で粘度750,000〜1
.000,000cpsでほとんど流動性を示さないも
のであった。
8.1 parts of cocoa butter, 20.0 parts of whole milk powder, and 10.85 parts of tempered hard butter (melting point 35.0°C, trade name, Melano SS 200) were blended, and the oil content was 34.2% according to the conventional method. A tempered milk chocolate dough was obtained. Melts at 50-55°C and has a viscosity of 65,00
The dough at 0 cps was fed at a constant rate of 120 kg per hour into a scraping-type stirring heat exchanger in which 40° C. hot water was circulated through the jacket part using a Moino pump. At this time, the temperature of the dough at the outlet of the heat exchanger was 40°C ± 0.4°C. Next, brine at 10°C was circulated through the dough through a pipe connected to the outlet of the scraped-type stirring heat exchanger. 100-1 on the jacket part
The dough was fed into a 20-bottle stirring heat exchanger and cooled to an outlet temperature of 26 to 25.8°C. The viscosity of the dough at that time was 300.000 cps to 400.000 cps. Brine was further circulated through a vibrator connected to the bottle-shaped stirring heat exchanger outlet [1], and the dough was fed into an oak mixer (C9M type continuous cake mixer) at -25° C. through the jacket section, which was stirred at 40 rpm. At this time, the pressure is 11 kg/cm2 at the inlet of the stirring section and 3 kg/cm2 at the outlet of the stirring section.
It was m2. J! jl Stirring section inlet force 15kg/c
3. m2 of nitrogen gas is passed through the flow rate regulator at a constant rate.
J at the rate of 2 U! It was then discharged. The dough thus obtained has a viscosity of 750,000 to 1 at a temperature of 25.8℃.
.. 000,000 cps and showed almost no fluidity.

該生地はそのまま15℃、風速7履/秒の冷風を循環せ
る冷却箱中に移し、15分間冷却固化した後、ナイフで
切り 20HX 150L X 25讐lImの長方体
に成形した製品とした。この製品は比重が0.78で元
のミルクチョコレート本来の茶褐色が薄い茶色となり、
しかも切削面はキメの細かい表面状態を呈し、軽い柔か
い食感を感じさせる好ましい外観を?していた。又、割
面も肉眼的に気泡跡がわからない程度の直径0.2■以
下の気泡が均一に分散していた。この製品を喫食したと
ころ、通常の板チョコの様な硬いかみ出しの南当りは全
ごなく、軟らかい噛み心地であり、しかも舌ざわりが滑
らかで口溶けの優れたものであった。
The dough was transferred as it was into a cooling box in which cold air was circulated at 15° C. at a wind speed of 7 shoes/second, cooled and solidified for 15 minutes, and then cut with a knife into a rectangular product measuring 20H x 150L x 25mm. This product has a specific gravity of 0.78, and the original milk chocolate's original brown color becomes light brown.
Moreover, the cut surface exhibits a fine-grained surface condition, giving it a pleasant appearance with a light and soft texture. Was. Also, on the cut surface, bubbles with a diameter of 0.2 square centimeters or less were uniformly dispersed, with no trace of bubbles visible to the naked eye. When I ate this product, I found that it had a soft texture without the hard bite of regular chocolate bars, and had a smooth texture and melted in the mouth.

−・方、上記配合のミルクチョコレート生地に対し溶解
したテトラグリセリンペンタステアレート(SYグリス
ター)を0.5%添加配合し、以下同一の操作を繰り返
して得た製品は比重が0.69であり、E配回様に外観
1食感共にすぐれた製品であったが、特に色調はさらに
白っぽくかみ心地はさらに軟らかくなっていた。この様
にして得た製品類を3ケ月以上室温に保存したが、全く
プルームを生ぜず、食感、風味、味等も全く変化してい
ないことがわかった。
- - The product obtained by adding 0.5% of dissolved tetraglycerin pentastearate (SY Glister) to the milk chocolate dough of the above composition and repeating the same operation has a specific gravity of 0.69. Although the product was excellent in both appearance and texture, the color was whitish and the texture was softer. Although the products thus obtained were stored at room temperature for more than three months, it was found that no plumes were formed and the texture, flavor, taste, etc. did not change at all.

Claims (5)

【特許請求の範囲】[Claims] (1)溶融した油脂性菓子生地を適宜攪拌冷却しつつ粘
度300,000〜500,000cps程度に調整し
た後、該生地を適宜量の不活性ガスと共にオークス・ミ
キサー等の冷却ジャケット付連続加圧泡立て攪拌装置内
に連続的に送入し、該生地を冷却しつつ攪拌して不活性
ガスを該生地内に均一に分散させ、次いで常圧中に排出
することにより径0.3mm程度以下の気泡を均一に含
有し、比重が0.6〜0.8の低密度油脂性菓子生地を
調製し、しかる後常法により成形、冷却固化することを
特徴とする低密度油脂性菓子の製造方法。
(1) After adjusting the viscosity of the molten oil-based confectionery dough to approximately 300,000 to 500,000 cps while appropriately stirring and cooling, the dough is continuously pressurized with an appropriate amount of inert gas using a cooling jacket such as an Oaks mixer. The dough is continuously fed into a foaming and stirring device, stirred while cooling to uniformly disperse the inert gas within the dough, and then discharged into normal pressure to form a dough with a diameter of about 0.3 mm or less. A method for producing a low-density oil-based confectionery, which comprises preparing a low-density oil-based confectionery dough that uniformly contains air bubbles and has a specific gravity of 0.6 to 0.8, and then molding it by a conventional method and solidifying it by cooling. .
(2)窒素ガス、炭酸ガス等の不活性と共に必要に応じ
て揮発性香料を連続的に圧入する特許請求の範囲第1項
に記載の低密度油脂性菓子の製造方法。
(2) The method for producing a low-density oil-based confectionery according to claim 1, in which inert gas such as nitrogen gas or carbon dioxide gas and, if necessary, a volatile flavoring agent are continuously injected.
(3)油脂性菓子生地を標準状態換算で1.2〜2.5
倍容量の不活性ガスと共に加圧連続攪拌装置内に連続的
に送入する特許請求の範囲第1項に記載の低密度油脂性
菓子の製造方法。
(3) Oil-based confectionery dough is 1.2 to 2.5 in standard condition.
2. The method for producing a low-density oil-based confectionery according to claim 1, which comprises continuously feeding the inert gas into a pressurized continuous stirring device together with double the volume of inert gas.
(4)油脂性菓子生地として予め乳化剤を0.5%程度
配合したものを使用する特許請求の範囲第1項に記載の
低密度油脂性菓子の製造方法。
(4) The method for producing a low-density oil-based confectionery according to claim 1, wherein the oil-based confectionery dough contains about 0.5% of an emulsifier in advance.
(5)乳化剤がテトラグリセリンペンタステアレートで
ある特許請求の範囲第4項に記載の低密度油脂性菓子の
製造方法。
(5) The method for producing a low-density fat-based confectionery according to claim 4, wherein the emulsifier is tetraglycerol pentasteate.
JP61192844A 1986-08-20 1986-08-20 Production of low-density fat and oil cake Granted JPS6349040A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61192844A JPS6349040A (en) 1986-08-20 1986-08-20 Production of low-density fat and oil cake

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61192844A JPS6349040A (en) 1986-08-20 1986-08-20 Production of low-density fat and oil cake

Publications (2)

Publication Number Publication Date
JPS6349040A true JPS6349040A (en) 1988-03-01
JPH0338820B2 JPH0338820B2 (en) 1991-06-11

Family

ID=16297915

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61192844A Granted JPS6349040A (en) 1986-08-20 1986-08-20 Production of low-density fat and oil cake

Country Status (1)

Country Link
JP (1) JPS6349040A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0494384A2 (en) * 1990-12-10 1992-07-15 Meiji Seika Kaisha Ltd. Process for the manufacture of chocolate confectionery with fine gas bubbles entrapping a fatty cream base
JPH10150916A (en) * 1996-11-20 1998-06-09 Fuji Oil Co Ltd Chocolate composition and its production
JP2009060848A (en) * 2007-09-06 2009-03-26 Nisshin Flour Milling Inc Method for producing doughnut-like food
JP2010207196A (en) * 2009-03-12 2010-09-24 Morinaga & Co Ltd Aerated chocolate, baked aerated chocolate, and method for producing the same
US8293313B2 (en) 2005-10-26 2012-10-23 Compagnie Gervais Danone Microfoamed fruit or vegetable puree and method for preparing same
JP2013158312A (en) * 2012-02-07 2013-08-19 Sugihara Craft:Kk Method for making confectionery/cake

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0494384A2 (en) * 1990-12-10 1992-07-15 Meiji Seika Kaisha Ltd. Process for the manufacture of chocolate confectionery with fine gas bubbles entrapping a fatty cream base
JPH04234948A (en) * 1990-12-10 1992-08-24 Meiji Seika Kaisha Ltd Production of foam-containing oily cream-containing chocolate
EP0494384A3 (en) * 1990-12-10 1994-02-23 Meiji Seika Kaisha
US5370888A (en) * 1990-12-10 1994-12-06 Meiji Seika Kaisha, Ltd. Process for the manufacture of chocolate confectionary by entrapping a fatty cream with fine gas bubbles therein
JPH10150916A (en) * 1996-11-20 1998-06-09 Fuji Oil Co Ltd Chocolate composition and its production
US8293313B2 (en) 2005-10-26 2012-10-23 Compagnie Gervais Danone Microfoamed fruit or vegetable puree and method for preparing same
JP2009060848A (en) * 2007-09-06 2009-03-26 Nisshin Flour Milling Inc Method for producing doughnut-like food
JP4642051B2 (en) * 2007-09-06 2011-03-02 日清製粉株式会社 Manufacturing method of donut-like food
JP2010207196A (en) * 2009-03-12 2010-09-24 Morinaga & Co Ltd Aerated chocolate, baked aerated chocolate, and method for producing the same
JP2013158312A (en) * 2012-02-07 2013-08-19 Sugihara Craft:Kk Method for making confectionery/cake

Also Published As

Publication number Publication date
JPH0338820B2 (en) 1991-06-11

Similar Documents

Publication Publication Date Title
US5126160A (en) Aqueous foaming compostion and method for homogenizingly incorporating water into lipophilic materials
KR100514337B1 (en) Hollow cakes containing puffed chocolate and process for producing the same
CA2019973C (en) Aqueous foaming composition and method for homogeneously incorporating water into lipophilic materials
JP3460478B2 (en) Process for producing foamable oil-in-water emulsified fats and oils and emulsified fats and oils
JPH01144934A (en) Preparation of cellular chocolate
JPH05111350A (en) Production of confection using ganasch
JPS6349040A (en) Production of low-density fat and oil cake
JPS6328355A (en) Foam-containing chocolate cake and production thereof
WO2002076225A1 (en) Whip chocolate products and process for producing the same
JPH0616676B2 (en) Multicellular frozen dessert material
JP4711898B2 (en) Composite chocolate and method for producing the same.
JPS62275648A (en) Gas-containing chocolate and production thereof
JPS63202341A (en) Cellular chocolate and production thereof
JP2003009774A (en) Air bubble-containing oil-and-fat composition which is soft even in frozen state
Pugh et al. A short overview of bubbles in foods and chocolate
MXPA01005314A (en) Improvements in confectionery manufacture.
JP5697133B2 (en) Method for producing foamable oil-in-water emulsified oil / fat composition for chilled whipped cream
JPS6058037A (en) Making of foaming chocolate
JP2529728B2 (en) Filling material manufacturing method
JPH1075724A (en) Foamed dessert and its production
JP3420865B2 (en) Whipping cream
JPH04104764A (en) Preparation of air-containing chocolate cake
JPS5922504B2 (en) Method for producing multicellular food
JPH0670689A (en) Production of soft ice
JPH01285154A (en) Production of plastic in-oil fine particle dispersing type food having void

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term