JPH054058B2 - - Google Patents

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Publication number
JPH054058B2
JPH054058B2 JP59076283A JP7628384A JPH054058B2 JP H054058 B2 JPH054058 B2 JP H054058B2 JP 59076283 A JP59076283 A JP 59076283A JP 7628384 A JP7628384 A JP 7628384A JP H054058 B2 JPH054058 B2 JP H054058B2
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JP
Japan
Prior art keywords
oil
confectionery
parts
fat
component
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 - Lifetime
Application number
JP59076283A
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Japanese (ja)
Other versions
JPS60221035A (en
Inventor
Shoshi Maruzeni
Hideo Yokobori
Toshimichi Yanagihara
Nozomi Yasuda
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.)
Adeka Corp
Original Assignee
Asahi Denka Kogyo KK
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Filing date
Publication date
Application filed by Asahi Denka Kogyo KK filed Critical Asahi Denka Kogyo KK
Priority to JP59076283A priority Critical patent/JPS60221035A/en
Publication of JPS60221035A publication Critical patent/JPS60221035A/en
Publication of JPH054058B2 publication Critical patent/JPH054058B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、製菓用油脂組成物、さらに詳しく
は、非常にシヤープな融解特性を有し、また、ラ
ウリン型油脂或いはその加工油脂に類似の物性を
有する非ラウリン系油脂組成物に関するものであ
る。 ラウリン型油脂とは、ヤシ油、パーム核油、バ
バス油核等のようなラウリン酸基を主要成分とす
るグリセリドからなる油脂で、その特異な物性は
製菓用油脂として重要である。ラウリン型油脂或
いはその加工油脂は硬化速度が速く(速乾性)且
つ非常にシヤープに融解するという特徴があり、
冷菓、チルド菓子製品或いはエンローバ、フイリ
ング菓子製品等では必須の油脂成分と考えられて
いる。しかしながら、ラウリン型油脂の最大の欠
点は、この加水分解臭である。加水分解の起きる
主な原因は微生物の作用によるものであるが、わ
ずかな程度の加水分解で悪臭を呈する。これは加
水分解で遊離するラウリン酸を中心とする短・中
鎖脂肪酸が嘔吐を催させる特異な臭いを有してい
るためである。ラウリン型油脂のもうひとつの欠
点は、カカオ脂との配合性が非常に悪いという点
である。最近はチヨコレートを使用した複合菓子
類が多くなつているが、チヨコレート中の油脂成
分であるカカオ脂との配合性が悪いと、チヨコレ
ート利用複合菓子類の製造の際、配合上の種々の
制限をうけ、自由な商品設計が出来ない。さらに
又、ラウリン型油脂は需給バランスが不安定で、
しばしば高騰し、その度に用途毎のより安価な代
替油脂が求められてきたわけである。 本発明は、非常にシヤープな融解特性を有し、
また、ラウリン型油脂に類似の物性を具備し、且
つ上記のラウリン型油脂の種々の欠陥の除去され
た製菓用油脂組成物を提供するものである。 即ち、本発明の製菓用油脂組成物は、下記のA
成分60〜95重量%、下記のB成分5〜40重量%、
及び下記のC成分0〜2重量%より成り、固体脂
含有率が20℃で30〜60、25℃で25〜40、30℃で0
〜20、33℃で0〜3、35℃で0〜1、37℃で0で
あることを特徴としている。 A成分:ヨウ素価が40〜50であるパーム油の分
別中融点画分 B成分:コクム脂、イリツペ脂、サル脂、マン
ゴー脂、マウア脂、シア脂及びこれらの分別中融
点画分からなる群から選ばれた一種又は二種以上
の配合油脂 C成分:油溶性乳化剤 以下に本発明の製菓用油脂組成物について詳述
する。 本発明の製菓用油脂組成物は、その構成油脂成
分から明らかなように、飽和脂肪酸が実質的にパ
ルミチン酸基、ステアリン酸基、アラキン酸基よ
りなり、不飽和脂肪酸基が実質的にオレイン酸
基、リノール酸基よりなる。従つて、ラウリン型
油脂の脂肪酸組成とは全く異なり、加水分解臭が
発生することはない。 本発明の製菓用油脂組成物の主体をなすA成
分、つまりヨウ素価が40〜50であるパーム油の分
別中融点画分は、分別プロセスにより製造され
る。このA成分の製造方法の例についてその概要
を以下に示す。 パーム油より、先ず、ウインターリング或いは
溶剤分別により高融点画分を除去し、実質的に三
飽和グリセリドを含有しない画分(パームオレイ
ン)を得る。次に、これを溶剤分別により中融点
画分(本発明で用いられるA成分)と低融点画分
に分別する。この溶剤分別の際、該中融点画分の
ヨウ素価が40〜50になるように分別条件を設定す
る必要がある。該分別条件は、用いる溶剤により
異なる。例えば、溶剤としてヘキサンを用いる場
合は、油脂1部に対しヘキサンを0.5〜4.0部用
い、−20℃〜−5℃の温度で分別する。アセトン
を用いる場合は、油脂1部に対しアセトンを0.5
〜7.0部用い、−5℃〜+8℃の温度で分別する。
分別プロセスは上記以外にも各種のプロセスが使
用できる。 本発明で用いられる上記A成分のヨウ素価は、
従来のハードバター原料用のパーム中融点画分の
ヨウ素価が33〜36であるのに対し、40〜50である
点が異なる。つまり、上記A成分は従来のハード
バター原料用のパーム中融点画分に比較して、不
飽和度が大である。分別により得られる上記A成
分のトリグセリド組成は必ずしも明らかではない
が、従来のハードバター原料用のパーム中融点画
分がジ飽和モノオレインが主体であるのに対し、
ジ飽和モノオレインに加えジ飽和モノリノレイン
から成ると思われる。上記A成分のリノール酸含
量は、従来のハードバター用原料用のパーム中融
点画分のそれの約3倍である。 本発明においては、A成分として、ヨウ素価が
40〜50のパーム油の中融点画分に従来のハードバ
ター原料用のパーム中融点画分(ヨウ素価33〜
36)を、ヨウ素価が40以下にならない範囲で一部
配合したものを使用することもできる。 また、本発明の製菓用油脂組成物を構成するB
成分は、コクム脂、イリツプ脂、サル脂、マンゴ
ー脂、マウア脂、シア脂及びこれらの分別中融点
画分からなる群から選ばれた一種或いは二種以上
の配合油脂である。 コクム脂、イリツペ脂は分別しないで単なる精
製を行つて直接使用し得る。サル脂、マンゴー
脂、マウア脂、シア脂は分別中融点画分を使用す
ることが望ましい。これらの油脂は1,3−ステ
アロ−2−オレイン(StOSt)或いは1−(3−)
パルミト−2−オレオ−3−(1−)ステアリン
(POS、SOP)をその中融点画分に含有してお
り、前記A成分に配合することにより各種製菓用
素材との配合性が非常に良好となる。 また、本発明の製菓用油脂組成物に加えること
のできるC成分としての油溶性乳化剤としては、
通常の混合操作で油脂に均一混合可能な乳化剤
で、例えば、モノグリセリドのようなグリセロー
ル脂肪酸エステル、ポリグリセリン脂肪酸エステ
ル、レシチン等が挙げられる。具体的には、酢酸
モノグリセリド、乳酸モノグリセリド、クエン酸
モノグリセリド、ジアセチル酒石酸モノグリセリ
ド、酒石酸モノグリセリド、コハク酸モノグリセ
リド、ポリグリセリン縮合リシノレイン酸エステ
ル、リンゴ酸モノグリセリド等が挙げられる。こ
れらの乳化剤は本発明の油脂組成物の必須成分で
はないが、これを0〜2重量%の範囲内で有効量
使用することにより本発明の製菓用油脂組成物の
粘性を変え、各種製菓用組成物の製造の際の作業
性を一層改善することができる。特に、ヤシ油に
類似の粘性特性を出すにはレシチンとポリグリセ
リン縮合リシノレイン酸エステルの併用がよい。 上記の、A成分、B成分及びC成分より成る、
本発明の製菓用油脂組成物の固体脂含有率は20℃
で30〜60、25℃で25〜40、30℃で0〜20、33℃で
0〜3、35℃で0〜1、37℃で0であることを特
徴としている。従つて、本発明の製菓用油脂組成
物は25℃以下では固型を保持しているが、30℃で
は固型が保持できないか或いは溶解するという特
徴を有している。 本発明の製菓用油脂組成物は、−10〜−20℃程
度で保管されて食される、いわゆる冷菓用、或い
は0〜5℃程度で保管されて食されるチルド製品
用、或いは夏期以外の常温流通品における、セン
タークリーム用又はフイリング用油脂に適する。
また、各種製菓用素材製造の際の配合性が非常に
よく、且つ製品の口溶けも良好で清涼感を与え
る。 尚、本発明において固体脂含有率は、25℃で7
日間の調質条件以外は常法(A.O.C.S.
Recommended Practice Cd 16−81 Solid Fat
Content)に従つて、PRAXIS MODES SFC−
900を用いて測定したものである。 以下に参考例、実施例及び使用例を挙げ、本発
明をさらに詳細に説明する。 参考例 1 アルカリ脱酸及び漂泊したパーム油(ヨウ素価
53.4)1部(重量基準、以下同様)にn−ヘキサ
ン0.1部を混合し、42℃に保持して均一ミセラ溶
解物を得た。該均一ミセラ溶解物を20℃まで冷却
した。次に予め15℃に冷却したn−ヘキサン0.3
部を加え、15分間撹拌保持した後、結晶と瀘液を
濾別した。分離された結晶は、15℃のn−ヘキサ
ン0.3部で洗浄した。該洗浄液と瀘液を混合し、
溶剤を留去した。結晶中の溶剤も同様に留去し
た。該結晶部(C)の収率は12.5%(重量基準、以下
同様)、該瀘液部(F)の収率は87.5%であつた。 上記瀘液部(F)に1部n−ヘキサン0.8部を混合
し、40℃に保持して均一ミセラ溶剤物を得た。該
均一ミセラ溶解物を−7℃まで冷却した。次に予
め−12℃に冷却したn−ヘキサン0.7部を加え撹
拌した後、結晶と瀘液を濾別した。結晶は−12℃
のn−ヘキサン1部で洗浄した。結晶及び瀘液よ
り溶剤を留去した。該結晶部(CF)の収率は
43.7%、該瀘液部(FF)の収率は56.3%であつ
た。該結晶部(CF)のヨウ素価は45.0であつた。
ここに結晶部(CF)はA成分に相当する分画物
である。 参考例 2 アルカリ脱酸及び漂泊したパーム油(ヨウ素価
53.4)1部にn−ヘキサン4部を混合し、40℃に
保持して均一ミセラ溶解物を得た。該均一ミセラ
溶解物を−17℃に冷却し、撹拌しながら60分間こ
の温度に保持した後、濾別及び溶剤の留去を行
い、結晶部(C)63.6%、瀘液部(F)36.4%を得た。 上記結晶部(C)1部にn−ヘキサン4部を混合
し、40℃に保持して均一ミセラ溶解物を得た。該
均一ミセラ溶解物を1℃まで冷却し、撹拌しなが
ら30分間この温度にした後、結晶と瀘液を濾別し
た。結晶は−5℃のn−ヘキサン0.3部で洗浄し
た。洗浄液は瀘液といつしよにして瀘液とした。
該結晶及び瀘液より溶剤を留去し、結晶部(CC)
21.3%及び瀘液部(FC)78.7%を得た。該瀘液部
(FC)のヨウ素価は47.0であつた。ここに結晶部
(FC)はA成分に相当する分画物である。 参考例 3 マレーシアより輸入したパームオレイン〔ヨウ
素価57.4(ウインターリング方法によつて製造さ
れたパーム軟質油)〕1部にn−ヘキサン1部を
混合し、40℃に保持して均一ミセラ溶解物を得
た。該均一ミセラ溶解物を−9℃まで冷却した。
次に予め−13℃に冷却したn−ヘキサン0.7部を
加え撹拌した後、結晶と瀘液を濾別した。結晶は
−13℃のn−ヘキサン2部で洗浄した。結晶及び
瀘液より溶剤を留去した。該結晶部(CF)の収
率は41.5%、該瀘液部(FF)の収率は58.5%であ
つた。該結晶部(CF)のヨウ素価は42.8であつ
た。ここに結晶部(CF)はA成分に相当する分
画物である。 参考例 4 マレーシアより輸入したパームオレイン〔ヨウ
素価58.1(ウインターリング方法によつて製造さ
れたパーム軟質油)〕1部にアセトン1.2部を混合
し、40℃に保持して均一ミセラ溶解物を得た。該
均一ミセラ溶解物を5.8℃まで冷却した。次に予
め2℃に冷却したアセトン0.7部を加え撹拌した
後、結晶と瀘液を濾別した。結晶は2℃のアセト
ン1部で洗浄した。結晶及び瀘液より溶剤を留去
した。該結晶部(CF)の収率は46.7%、該瀘液
部(FF)の収率は53.3%であつた。該結晶部
(CF)のヨウ素価は49.7であつた。ここに結晶部
(CF)はA成分に相当する分画物である。 参考例 5 アルカリ脱酸及び漂泊したパーム油(ヨウ素価
53.4)1部(重量基準、以下同様)にn−ヘキサ
ン0.1部を混合し、42℃に保持して均一ミセラ溶
解物を得た。該均一ミセラ溶解物を20℃まで冷却
した。次に予め15℃に冷却したn−ヘキサン0.3
部を加え、15分間撹拌保持した後、結晶と瀘液を
濾別した。分離された結晶は、15℃のn−ヘキサ
ン0.3部で洗浄した。該洗浄液と瀘液を混合し、
溶剤を留去した。結晶中の溶剤も同様に留去し
た。該結晶部(C)の収率は12.5%(重量基準、以下
同様)、該瀘液部(F)の収率は87.5%であつた。 上記瀘液部(F)1部にn−ヘキサン2.5部を混合
し、40℃に保持して均一ミセラ溶解物を得た。該
均一ミセラ溶解物を−10℃まで冷却した。次に予
め−15℃に冷却したn−ヘキサン0.7部を加え撹
拌した後、結晶と瀘液を濾別した。結晶は−15℃
のn−ヘキサン2部で洗浄した。結晶及び瀘液よ
り溶剤を留去した。該結晶部(CF)の収率は
28.7%、該瀘液部(FF)の収率は71.3%であつ
た。該結晶部(CF)のヨウ素価は35.0であつた。
ここに結晶部(CF)はカカオバター代用脂の原
料となるパーム中融点画分である。 参考例 6 精製マウア脂1部にアセトン3.5部を混合溶解
した後、23℃まで冷却し、その温度で40分間保持
した後、結晶部を濾別除去した。瀘液部はさらに
冷却して、0℃で1時間保持した後、結晶部と瀘
液部とを濾別した。さらに該結晶部1部にアセト
ン3.5部を混合溶解した後、5℃まで冷却し、そ
の温度で1時間保持した後、濾別により結晶部と
瀘液部を分離した。該結晶部がマウア中融点部
で、収率は対精製マウア脂で25.6%、またヨウ素
価は38.0であつた。 参考例 7 精製シア脂1部にアセトン3部を混合した後、
室温に放置してガム状物質及び高融点画分からな
る結晶を生成沈澱させ、デカンテーシヨンにより
上澄液を分取した。該上澄液より、溶剤を留去
し、脱ガムシア脂を得た。該脱ガムシア脂1部に
ヘキサン4部を混合溶解後−7℃まで冷却し、そ
の温度で30分間保持した後、結晶部と瀘液部を濾
別した。結晶部は−12℃のヘキサン2部で洗浄し
た。結晶部つまりシアステアリンの収率は対脱ガ
ムシア脂で37%であつた。また、該シアステアリ
ンのヨウ素価は33.5であつた。 実施例 1 参考例1で得た精製CF画分85部に精製コクム
脂15部を配合し、製菓用油脂組成物を調製した。
該製菓用油脂組成物のヨウ素価と固体脂含有率を
第1表に示した。 実施例 2 参考例2で得た精製FC画分80部に精製イリツ
ペ脂20部を配合し、製菓用油脂組成物を調製し
た。該製菓用油脂組成物のヨウ素価と固体脂含有
率を第1表に示した。 実施例 3 参考例3で得た精製CF画分70部に精製サル脂
30部を配合し、製菓用油脂組成物を調製した。該
製菓用油脂組成物のヨウ素価と固体脂含有率を第
1表に示した。 実施例 4 参考例4で得た精製CF画分65部に精製マンゴ
ー脂35部及びステアリン酸モノグリセリド0.2部
を配合し、製菓用油脂組成物を調製した。該製菓
用油脂組成物のヨウ素価と固体脂含有率を第1表
に示した。 実施例 5 参考例4で得た精製CF画分55部に参考例5で
得た精製CF画分35部を配合し、さらに参考例6
で得た精製マウア中融点画分10部及びレシチン
0.2部、ポリグリセリン縮合リシノレイン酸エス
テル0.2部を配合し、製菓用油脂組成物を調製し
た。該製菓用油脂組成物のヨウ素価と固体脂含有
率を第1表に示した。 実施例 6 参考例3で得た精製CF画分85部に参考例7で
得た精製シアステアリン15部及びレシチン0.2部、
ポリグリセリン縮合リシノレイン酸エステル0.2
部を配合し、製菓用油脂組成物を調製した。該製
菓用油脂組成物のヨウ素価と固体脂含有率を第1
表に示した。 実施例 7 参考例4で得た精製CF画分90部に精製マンゴ
ー脂10部及びレシチン0.2部、ポリグリセリン縮
合リシノレイン酸エステル0.2部を配合し、製菓
用油脂組成物を調製した。該製菓用油脂組成物の
ヨウ素価と固体脂含有率を第1表に示した。
The present invention relates to an oil and fat composition for confectionery, and more particularly to a non-lauric oil and fat composition that has very sharp melting characteristics and physical properties similar to lauric oil or its processed oil. Lauric type fats and oils are fats and oils consisting of glycerides whose main component is lauric acid groups, such as coconut oil, palm kernel oil, babassu oil kernels, etc., and their unique physical properties are important as fats and oils for confectionery. Lauric type oils and their processed oils have the characteristics of fast curing speed (quick drying) and very sharp melting.
It is considered to be an essential fat and oil component in frozen desserts, chilled confectionery products, enrobers, filled confectionery products, etc. However, the biggest drawback of lauric oils and fats is this hydrolyzed odor. The main cause of hydrolysis is the action of microorganisms, but even a small amount of hydrolysis causes a bad odor. This is because short- and medium-chain fatty acids, mainly lauric acid, liberated by hydrolysis have a unique odor that induces vomiting. Another drawback of lauric oils and fats is that they have very poor compatibility with cocoa butter. Recently, there have been an increase in the number of composite confectioneries using tiyocolate, but due to the poor compatibility with cacao butter, which is an oil component in tiyocolate, there are various restrictions on the formulation when manufacturing composite confectionery using tiyocolate. However, it is not possible to freely design products. Furthermore, the supply and demand balance for lauric oils and fats is unstable,
Prices often rise, and each time there is a need for cheaper alternative fats and oils for different uses. The present invention has very sharp melting characteristics,
Another object of the present invention is to provide an oil and fat composition for confectionery that has physical properties similar to those of lauric oil and fat and is free from various defects of the above-mentioned lauric oil and fat. That is, the oil and fat composition for confectionery of the present invention has the following A.
Ingredients 60-95% by weight, Component B below 5-40% by weight,
The solid fat content is 30-60 at 20℃, 25-40 at 25℃, and 0 at 30℃.
-20, 0-3 at 33°C, 0-1 at 35°C, and 0 at 37°C. Component A: Fractionated mid-melting point fraction of palm oil with an iodine value of 40 to 50. Component B: From the group consisting of kokum butter, iritupe butter, sal fat, mango butter, maua butter, shea butter, and their fractionated mid-melting point fractions. One or more selected blended fats and oils Component C: Oil-soluble emulsifier The oil and fat composition for confectionery of the present invention will be described in detail below. As is clear from the constituent oil and fat components of the oil and fat composition for confectionery of the present invention, the saturated fatty acids consist essentially of palmitic acid groups, stearic acid groups, and arachidic acid groups, and the unsaturated fatty acid groups essentially consist of oleic acid groups. group, linoleic acid group. Therefore, the fatty acid composition is completely different from that of lauric oils and fats, and no hydrolysis odor is generated. Component A, which is the main component of the oil and fat composition for confectionery of the present invention, that is, the fractionated intermediate melting point fraction of palm oil having an iodine value of 40 to 50 is produced by a fractionation process. An outline of an example of the method for producing component A is shown below. First, a high melting point fraction is removed from palm oil by wintering or solvent fractionation to obtain a fraction (palm olein) that does not substantially contain trisaturated glycerides. Next, this is separated into a medium melting point fraction (component A used in the present invention) and a low melting point fraction by solvent fractionation. During this solvent fractionation, it is necessary to set the fractionation conditions so that the iodine value of the medium melting point fraction is 40 to 50. The separation conditions vary depending on the solvent used. For example, when hexane is used as a solvent, 0.5 to 4.0 parts of hexane is used for 1 part of oil and fat, and the fractionation is carried out at a temperature of -20°C to -5°C. When using acetone, add 0.5 parts of acetone to 1 part of fat.
~7.0 parts are used and fractionated at a temperature of -5°C to +8°C.
As the separation process, various processes other than those described above can be used. The iodine value of the above component A used in the present invention is:
The difference is that the iodine value of the palm medium melting point fraction used for conventional hard butter raw materials is 33 to 36, while it is 40 to 50. That is, the above-mentioned component A has a higher degree of unsaturation than the palm medium melting point fraction used as a conventional hard butter raw material. The triglyceride composition of the component A obtained by fractionation is not necessarily clear, but while the palm mid-melting point fraction for conventional hard butter raw materials is mainly composed of disaturated monoolein,
It appears to consist of disaturated monolinolein in addition to disaturated monoolein. The linoleic acid content of the above component A is about three times that of the palm medium melting point fraction used as a conventional raw material for hard butter. In the present invention, as the A component, the iodine value is
The medium melting point fraction of palm oil with an iodine value of 33 to 50 and the palm medium melting point fraction for conventional hard butter raw materials
36) may also be used, as long as the iodine value does not fall below 40. Further, B constituting the oil and fat composition for confectionery of the present invention
The ingredients are one or more blended fats and oils selected from the group consisting of kokum butter, irippu butter, monkey fat, mango butter, maua butter, shea butter, and their fractionated intermediate melting point fractions. Kokum fat and Iritzpe fat can be used directly after simple purification without being separated. For monkey fat, mango fat, maua butter, and shea butter, it is desirable to use fractionated intermediate melting point fractions. These fats and oils are 1,3-stearo-2-olein (StOSt) or 1-(3-)
Contains palmito-2-oleo-3-(1-) stearin (POS, SOP) in its medium melting point fraction, and by adding it to component A, it has very good compatibility with various confectionery materials. becomes. In addition, oil-soluble emulsifiers as component C that can be added to the oil and fat composition for confectionery of the present invention include:
Emulsifiers that can be uniformly mixed with fats and oils through normal mixing operations include, for example, glycerol fatty acid esters such as monoglycerides, polyglycerin fatty acid esters, and lecithin. Specifically, acetic acid monoglyceride, lactic acid monoglyceride, citric acid monoglyceride, diacetyl tartaric acid monoglyceride, tartaric acid monoglyceride, succinic acid monoglyceride, polyglycerin condensed ricinoleate, malic acid monoglyceride, and the like. These emulsifiers are not essential components of the oil and fat composition of the present invention, but by using them in an effective amount within the range of 0 to 2% by weight, the viscosity of the oil and fat composition for confectionery of the present invention can be changed, and it can be used for various confectionery products. Workability during production of the composition can be further improved. In particular, in order to achieve viscosity properties similar to those of coconut oil, a combination of lecithin and polyglycerin condensed ricinoleic acid ester is recommended. Consisting of the above A component, B component and C component,
The solid fat content of the confectionery oil and fat composition of the present invention is 20°C
30 to 60 at 25°C, 25 to 40 at 25°C, 0 to 20 at 30°C, 0 to 3 at 33°C, 0 to 1 at 35°C, and 0 at 37°C. Therefore, the oil and fat composition for confectionery of the present invention is characterized in that it retains its solid form at temperatures below 25°C, but either cannot retain its solid form or dissolves at 30°C. The oil and fat composition for confectionery of the present invention can be used for so-called frozen desserts that are stored and eaten at about -10 to -20°C, for chilled products that are stored and eaten at about 0 to 5°C, or for products other than summer. Suitable for center cream or filling oils and fats for products sold at room temperature.
In addition, it is very compatible with the production of various confectionery materials, and the product melts well in the mouth, giving it a refreshing feel. In addition, in the present invention, the solid fat content is 7 at 25°C.
The conventional method (AOCS) except for the tempering conditions of
Recommended Practice Cd 16−81 Solid Fat
PRAXIS MODES SFC−
900. The present invention will be explained in further detail by referring to Reference Examples, Examples and Usage Examples below. Reference example 1 Alkali deoxidized and bleached palm oil (iodine value
53.4) 1 part (by weight, same hereinafter) was mixed with 0.1 part of n-hexane and maintained at 42°C to obtain a uniform micella melt. The homogeneous micellar melt was cooled to 20°C. Next, 0.3 n-hexane pre-cooled to 15℃
After stirring and maintaining the mixture for 15 minutes, the crystals and the filtrate were separated by filtration. The separated crystals were washed with 0.3 part of n-hexane at 15°C. Mixing the cleaning liquid and the filtration liquid,
The solvent was distilled off. The solvent in the crystals was also distilled off in the same way. The yield of the crystal part (C) was 12.5% (on a weight basis, the same applies hereinafter), and the yield of the filtrate part (F) was 87.5%. 1 part and 0.8 parts of n-hexane were mixed into the filtrate part (F) and maintained at 40°C to obtain a uniform micellar solvent. The homogeneous micellar melt was cooled to -7°C. Next, 0.7 part of n-hexane previously cooled to -12°C was added and stirred, and then the crystals and the filtrate were separated by filtration. Crystals at -12℃
was washed with 1 part of n-hexane. The solvent was distilled off from the crystals and filtrate. The yield of the crystal part (CF) is
The yield of the filtrate (FF) was 56.3%. The iodine value of the crystalline portion (CF) was 45.0.
Here, the crystal part (CF) is a fraction corresponding to component A. Reference example 2 Alkali deoxidized and bleached palm oil (iodine value
53.4) 1 part was mixed with 4 parts of n-hexane and kept at 40°C to obtain a homogeneous micellar melt. The homogeneous micellar melt was cooled to -17°C and maintained at this temperature for 60 minutes while stirring, and then filtered and the solvent was distilled off, resulting in a crystal part (C) of 63.6% and a filtrate part (F) of 36.4%. I got %. 4 parts of n-hexane was mixed with 1 part of the crystal part (C) and maintained at 40°C to obtain a homogeneous micellar melt. The homogeneous micellar melt was cooled to 1° C. and maintained at this temperature for 30 minutes with stirring, after which the crystals and filtrate were filtered off. The crystals were washed with 0.3 parts of n-hexane at -5°C. The cleaning solution was used as a filtrate.
The solvent was distilled off from the crystals and filtrate, and the crystal part (CC)
21.3% and filtrate (FC) 78.7%. The iodine value of the filtrate (FC) was 47.0. Here, the crystal part (FC) is a fraction corresponding to component A. Reference Example 3 One part of palm olein imported from Malaysia [iodine value 57.4 (palm soft oil produced by wintering method)] was mixed with one part of n-hexane and kept at 40°C to form a homogeneous micellar melt. I got it. The homogeneous micellar melt was cooled to -9°C.
Next, 0.7 part of n-hexane previously cooled to -13°C was added and stirred, and then the crystals and the filtrate were separated by filtration. The crystals were washed with 2 parts of n-hexane at -13°C. The solvent was distilled off from the crystals and filtrate. The yield of the crystal part (CF) was 41.5%, and the yield of the filtrate part (FF) was 58.5%. The iodine value of the crystalline portion (CF) was 42.8. Here, the crystal part (CF) is a fraction corresponding to component A. Reference Example 4 1 part of palm olein imported from Malaysia [iodine value 58.1 (palm soft oil produced by wintering method)] was mixed with 1.2 parts of acetone and kept at 40°C to obtain a homogeneous micellar melt. Ta. The homogeneous micellar melt was cooled to 5.8°C. Next, 0.7 part of acetone previously cooled to 2° C. was added and stirred, and then the crystals and the filtrate were separated by filtration. The crystals were washed with 1 part acetone at 2°C. The solvent was distilled off from the crystals and filtrate. The yield of the crystal part (CF) was 46.7%, and the yield of the filtrate part (FF) was 53.3%. The iodine value of the crystalline portion (CF) was 49.7. Here, the crystal part (CF) is a fraction corresponding to component A. Reference example 5 Alkaline deoxidized and bleached palm oil (iodine value
53.4) 1 part (by weight, same hereinafter) was mixed with 0.1 part of n-hexane and maintained at 42°C to obtain a uniform micella melt. The homogeneous micellar melt was cooled to 20°C. Next, 0.3 n-hexane pre-cooled to 15℃
After stirring and maintaining the mixture for 15 minutes, the crystals and the filtrate were separated by filtration. The separated crystals were washed with 0.3 part of n-hexane at 15°C. Mixing the cleaning liquid and the filtration liquid,
The solvent was distilled off. The solvent in the crystals was also distilled off in the same way. The yield of the crystal part (C) was 12.5% (on a weight basis, the same applies hereinafter), and the yield of the filtrate part (F) was 87.5%. 2.5 parts of n-hexane was mixed with 1 part of the above filtrate part (F) and maintained at 40°C to obtain a homogeneous micella melt. The homogeneous micellar melt was cooled to -10°C. Next, 0.7 part of n-hexane previously cooled to -15°C was added and stirred, and then the crystals and the filtrate were separated by filtration. Crystals at -15℃
Washed with 2 parts of n-hexane. The solvent was distilled off from the crystals and filtrate. The yield of the crystal part (CF) is
The yield of the filtrate (FF) was 71.3%. The iodine value of the crystalline portion (CF) was 35.0.
The crystalline part (CF) here is the mid-melting point fraction of palm, which is the raw material for cocoa butter substitute. Reference Example 6 After mixing and dissolving 3.5 parts of acetone in 1 part of purified Maua fat, the mixture was cooled to 23°C, held at that temperature for 40 minutes, and then the crystalline portion was removed by filtration. The filtrate portion was further cooled and held at 0° C. for 1 hour, and then the crystal portion and the filtrate portion were separated by filtration. Further, 3.5 parts of acetone was mixed and dissolved in 1 part of the crystalline portion, cooled to 5° C., maintained at that temperature for 1 hour, and separated into a crystalline portion and a filtrate portion by filtration. The crystalline part was the Maua medium melting point part, the yield was 25.6% based on purified Maua fat, and the iodine value was 38.0. Reference Example 7 After mixing 3 parts of acetone with 1 part of purified shea butter,
Crystals consisting of a gummy substance and a high melting point fraction were formed and precipitated by standing at room temperature, and the supernatant liquid was separated by decantation. The solvent was distilled off from the supernatant to obtain degummed shea fat. After mixing and dissolving 4 parts of hexane in 1 part of the degummed shea fat, the mixture was cooled to -7°C, held at that temperature for 30 minutes, and then the crystalline part and the filtrate part were separated by filtration. The crystal part was washed with 2 parts of hexane at -12°C. The yield of crystalline parts, that is, shea stearin, was 37% based on the degummed shea fat. Further, the iodine value of the shea stearin was 33.5. Example 1 15 parts of purified Kokum fat was blended with 85 parts of the purified CF fraction obtained in Reference Example 1 to prepare an oil and fat composition for confectionery.
Table 1 shows the iodine value and solid fat content of the oil and fat composition for confectionery. Example 2 20 parts of purified Iritzpe butter was blended with 80 parts of the purified FC fraction obtained in Reference Example 2 to prepare an oil and fat composition for confectionery. Table 1 shows the iodine value and solid fat content of the oil and fat composition for confectionery. Example 3 Purified monkey fat was added to 70 parts of the purified CF fraction obtained in Reference Example 3.
30 parts were blended to prepare an oil and fat composition for confectionery. Table 1 shows the iodine value and solid fat content of the oil and fat composition for confectionery. Example 4 35 parts of purified mango fat and 0.2 parts of stearic acid monoglyceride were blended with 65 parts of the purified CF fraction obtained in Reference Example 4 to prepare an oil and fat composition for confectionery. Table 1 shows the iodine value and solid fat content of the oil and fat composition for confectionery. Example 5 35 parts of the purified CF fraction obtained in Reference Example 5 was blended with 55 parts of the purified CF fraction obtained in Reference Example 4, and further 35 parts of the purified CF fraction obtained in Reference Example 6 were added.
10 parts of purified Maua medium melting point fraction obtained from and lecithin
An oil and fat composition for confectionery was prepared by blending 0.2 parts of polyglycerin condensed ricinoleic acid ester. Table 1 shows the iodine value and solid fat content of the oil and fat composition for confectionery. Example 6 15 parts of purified sheastearin obtained in Reference Example 7 and 0.2 parts of lecithin were added to 85 parts of the purified CF fraction obtained in Reference Example 3,
Polyglycerin condensed ricinoleate ester 0.2
A confectionery oil and fat composition was prepared. The iodine value and solid fat content of the confectionery oil and fat composition are
Shown in the table. Example 7 10 parts of purified mango fat, 0.2 parts of lecithin, and 0.2 parts of polyglycerin condensed ricinoleate were added to 90 parts of the purified CF fraction obtained in Reference Example 4 to prepare an oil and fat composition for confectionery. Table 1 shows the iodine value and solid fat content of the oil and fat composition for confectionery.

【表】 使用例 1 実施例1で調製した製菓用油脂組成物40部及び
ホワイトチヨコレート17部を約50℃で溶解均一物
にした。一方、ホンダン13部、70%ソルビトール
7部及びレシチン0.2部を約50℃で加熱撹拌し均
一にした後、マロンペースト18部を加え混合し、
さらに室温にて実施例1て調製した製菓用油脂組
成物7部を加え撹拌した。該混合物に、先に調製
した溶解均一物を加え、よく撹拌しながら20℃ま
で冷却した後、型に流し込み5℃で固化した。前
記実施例1で調製した製菓用油脂組成物は上記プ
ロセスできわめて配合性が良く、容易に均一配合
物となり、また該配合物は口溶けが非常に良好
で、油分が非常に多いにも拘らず、清涼感を与え
るものであり、各種製菓用素材として使用できる
ものであつた。 使用例 2 実施例2で調製した製菓用油脂組成物50部及び
ホワイトチヨコレート20部を混合溶解後、20℃ま
で冷却しよく撹拌した後、予め調製しておいたラ
ム酒6部、ブルーベリージヤム20部の混合物を加
え撹拌し均一にした後5℃で固化した。前記実施
例2で調製した製菓用油脂組成物は上記プロセス
できわめて配合性がよく、容易に均一配合物とな
り、また該配合物は口溶けが非常に良好で清涼感
を与えるものであつた。 使用例 3 実施例3で調製した製菓用油脂組成物50部及び
ホワイトチヨコレート20部を混合溶解後、20℃ま
で冷却しよく撹拌した後、予め調製しておいたラ
ム酒6部、オレンジジヤム24部の混合物を加え撹
拌し均一にした後5℃で固化した。前記実施例3
で調製した製菓用油脂組成物は上記プロセスでき
わめて配合性がよく、容易に均一配合物となり、
また該配合物は口溶けが非常に良好で清涼感を与
えるものであつた。 使用例 4 ウオルナツトプラリネ18部及び砂糖17部をロー
ルがけした後、ミルクチヨコレート17部及び実施
例4で調製した製菓用油脂組成物48部、レシチン
0.2部とともに45℃でよく撹拌した後、22℃まで
撹拌しながら冷却し、さらに、5℃で固化した。
前記実施例4で調製した製菓用油脂組成物は上記
プロセスできわめて配合性がよく、容易に均一配
合物となり、また該配合物は口溶けが良好で清涼
感を与えるものであつた。 使用例 5 実施例1で調製した製菓用油脂組成物の代わり
に実施例5で調製した製菓用油脂組成物を用いた
以外は使用例1と同様の手順で製菓用配合物を調
製した。前記実施例5で調製した製菓用油脂組成
物は上記プロセスできわめて配合性がよく、容易
に均一配合物となり、また該製菓用配合物は口溶
けが良好であつた。 使用例 6 実施例2で調製した製菓用油脂組成物の代わり
に実施例6で調製した製菓用油脂組成物を用いた
以外は使用例2と同様の手順で製菓用配合物を調
製した。前記実施例6で調製した製菓用油脂組成
物は上記プロセスできわめて配合性がよく、容易
に均一配合物となり、また該製菓用配合物は口溶
けが良好であつた。 使用例 7 実施例3で調製した製菓用油脂組成物の代わり
に実施例7で調製した製菓用油脂組成物を用いた
以外は使用例2と同様の手順で製菓用配合物を調
製した。前記実施例7で調製した製菓用油脂組成
物は上記プロセスできわめて配合性がよく、容易
に均一配合物となり、また該製菓用配合物は口溶
けが良好であつた。
[Table] Usage Example 1 40 parts of the oil and fat composition for confectionery prepared in Example 1 and 17 parts of white chiyocholate were dissolved to form a homogeneous substance at about 50°C. On the other hand, 13 parts of Hondan, 7 parts of 70% sorbitol, and 0.2 parts of lecithin were heated and stirred at about 50°C to make them uniform, and then 18 parts of marron paste was added and mixed.
Furthermore, 7 parts of the confectionery oil and fat composition prepared in Example 1 were added and stirred at room temperature. The previously prepared dissolved homogeneous mixture was added to the mixture, cooled to 20°C while stirring well, and then poured into a mold and solidified at 5°C. The oil and fat composition for confectionery prepared in Example 1 has very good blendability in the above process and can easily be made into a uniform blend, and the blend melts in the mouth very well, even though it has a very high oil content. It gave a refreshing feeling and could be used as an ingredient for various confectionery products. Usage Example 2 After mixing and dissolving 50 parts of the oil and fat composition for confectionery prepared in Example 2 and 20 parts of white chiyocollate, cool to 20°C and stir well, add 6 parts of rum prepared in advance and 20 parts of blueberry jam. The mixture was stirred to make it homogeneous and then solidified at 5°C. The oil and fat composition for confectionery prepared in Example 2 had excellent blendability in the above process and was easily formed into a uniform blend, and the blend melted in the mouth very well and gave a refreshing sensation. Usage Example 3 After mixing and dissolving 50 parts of the oil and fat composition for confectionery prepared in Example 3 and 20 parts of white chiyocollate, cool to 20°C and stir well, add 6 parts of rum prepared in advance and 24 parts of orange jam. The mixture was stirred to make it homogeneous and then solidified at 5°C. Said Example 3
The oil and fat composition for confectionery prepared in the above process has extremely good blendability and can easily be made into a homogeneous blend.
Moreover, the formulation melted in the mouth very well and gave a refreshing feeling. Usage example 4 After rolling 18 parts of walnut praline and 17 parts of sugar, 17 parts of milk chocolate, 48 parts of the confectionery fat composition prepared in Example 4, and lecithin.
After stirring thoroughly at 45°C with 0.2 part, the mixture was cooled to 22°C with stirring, and further solidified at 5°C.
The oil and fat composition for confectionery prepared in Example 4 had excellent blendability in the above process and was easily formed into a uniform blend, and the blend melted well in the mouth and gave a refreshing sensation. Use Example 5 A confectionery formulation was prepared in the same manner as in Use Example 1, except that the confectionery oil and fat composition prepared in Example 5 was used instead of the confectionery oil and fat composition prepared in Example 1. The oil and fat composition for confectionery prepared in Example 5 had excellent blendability in the above process, was easily formed into a homogeneous blend, and the confectionery composition melted well in the mouth. Use Example 6 A confectionery formulation was prepared in the same manner as in Use Example 2, except that the confectionery oil and fat composition prepared in Example 6 was used instead of the confectionery oil and fat composition prepared in Example 2. The oil and fat composition for confectionery prepared in Example 6 had excellent blendability in the above process, was easily formed into a homogeneous blend, and the confectionery composition melted well in the mouth. Use Example 7 A confectionery formulation was prepared in the same manner as in Use Example 2, except that the confectionery oil and fat composition prepared in Example 7 was used instead of the confectionery oil and fat composition prepared in Example 3. The oil and fat composition for confectionery prepared in Example 7 had excellent blendability in the above process, was easily formed into a homogeneous blend, and the confectionery composition melted well in the mouth.

Claims (1)

【特許請求の範囲】 1 下記のA成分60〜95重量%、下記のB成分5
〜40重量%、及び下記のC成分0〜2重量%より
成り、固体脂含有率が20℃で30〜60、25℃で25〜
40、30℃で0〜20、33℃で0〜3、35℃で0〜
1、37℃で0であることを特徴とする製菓用油脂
組成物。 A成分:ヨウ素価が40〜50であるパーム油の分
別中融点画分 B成分:コクム脂、イリツペ脂、サル脂、マン
ゴー脂、マウア脂、シア脂及びこれらの分別中融
点画分からなる群から選ばれた一種又は二種以上
の配合油脂 C成分:油溶性乳化剤
[Scope of Claims] 1 60 to 95% by weight of the following A component, the following B component 5
-40% by weight, and 0-2% by weight of the following C component, with a solid fat content of 30-60 at 20℃ and 25-60 at 25℃
40, 0-20 at 30℃, 0-3 at 33℃, 0-35℃
1. An oil and fat composition for confectionery, characterized by having a temperature of 0 at 37°C. Component A: Fractionated mid-melting point fraction of palm oil with an iodine value of 40 to 50. Component B: From the group consisting of kokum butter, iritupe butter, sal fat, mango butter, maua butter, shea butter, and their fractionated mid-melting point fractions. One or more selected blended oils and fats Component C: Oil-soluble emulsifier
JP59076283A 1984-04-16 1984-04-16 Fat or oil composition for confectionery Granted JPS60221035A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59076283A JPS60221035A (en) 1984-04-16 1984-04-16 Fat or oil composition for confectionery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59076283A JPS60221035A (en) 1984-04-16 1984-04-16 Fat or oil composition for confectionery

Publications (2)

Publication Number Publication Date
JPS60221035A JPS60221035A (en) 1985-11-05
JPH054058B2 true JPH054058B2 (en) 1993-01-19

Family

ID=13600965

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59076283A Granted JPS60221035A (en) 1984-04-16 1984-04-16 Fat or oil composition for confectionery

Country Status (1)

Country Link
JP (1) JPS60221035A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0734714B2 (en) * 1986-05-01 1995-04-19 旭電化工業株式会社 Method for producing fat composition
DK119092D0 (en) * 1992-09-25 1992-09-25 Aarhus Oliefabrik As SURFACE TREATMENT AGENT
JP3371465B2 (en) * 1993-05-21 2003-01-27 鐘淵化学工業株式会社 Melting chocolates
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GB925805A (en) * 1958-06-11 1963-05-08 Unilever Ltd Improvements in or relating to cocoa butter substitutes

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JPS60221035A (en) 1985-11-05

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