JPH0347137B2 - - Google Patents
Info
- Publication number
- JPH0347137B2 JPH0347137B2 JP58005459A JP545983A JPH0347137B2 JP H0347137 B2 JPH0347137 B2 JP H0347137B2 JP 58005459 A JP58005459 A JP 58005459A JP 545983 A JP545983 A JP 545983A JP H0347137 B2 JPH0347137 B2 JP H0347137B2
- Authority
- JP
- Japan
- Prior art keywords
- oil
- water
- margarine
- fat composition
- acid ester
- 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
Links
- 239000000203 mixture Substances 0.000 claims description 24
- -1 ricinoleic acid ester Chemical class 0.000 claims description 19
- 238000004519 manufacturing process Methods 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 13
- 239000003995 emulsifying agent Substances 0.000 claims description 9
- 229960003656 ricinoleic acid Drugs 0.000 claims description 8
- FEUQNCSVHBHROZ-UHFFFAOYSA-N ricinoleic acid Natural products CCCCCCC(O[Si](C)(C)C)CC=CCCCCCCCC(=O)OC FEUQNCSVHBHROZ-UHFFFAOYSA-N 0.000 claims description 8
- 235000021122 unsaturated fatty acids Nutrition 0.000 claims description 8
- 229930006000 Sucrose Natural products 0.000 claims description 6
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 6
- 229930195729 fatty acid Natural products 0.000 claims description 6
- 239000000194 fatty acid Substances 0.000 claims description 6
- 239000005720 sucrose Substances 0.000 claims description 6
- 239000003921 oil Substances 0.000 description 50
- 239000003925 fat Substances 0.000 description 33
- 235000019197 fats Nutrition 0.000 description 29
- 235000019198 oils Nutrition 0.000 description 28
- 235000013310 margarine Nutrition 0.000 description 20
- 239000003264 margarine Substances 0.000 description 18
- 239000012071 phase Substances 0.000 description 16
- 235000008429 bread Nutrition 0.000 description 9
- 239000000839 emulsion Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 8
- 239000008346 aqueous phase Substances 0.000 description 7
- 235000009508 confectionery Nutrition 0.000 description 7
- 238000001816 cooling Methods 0.000 description 6
- 239000000796 flavoring agent Substances 0.000 description 5
- 235000014593 oils and fats Nutrition 0.000 description 5
- 238000004090 dissolution Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 239000007762 w/o emulsion Substances 0.000 description 4
- 238000004945 emulsification Methods 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 238000010791 quenching Methods 0.000 description 3
- WBHHMMIMDMUBKC-XLNAKTSKSA-N ricinelaidic acid Chemical compound CCCCCC[C@@H](O)C\C=C\CCCCCCCC(O)=O WBHHMMIMDMUBKC-XLNAKTSKSA-N 0.000 description 3
- 238000004904 shortening Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 235000002316 solid fats Nutrition 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- JNYAEWCLZODPBN-JGWLITMVSA-N (2r,3r,4s)-2-[(1r)-1,2-dihydroxyethyl]oxolane-3,4-diol Chemical compound OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O JNYAEWCLZODPBN-JGWLITMVSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 150000005690 diesters Chemical class 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 235000013355 food flavoring agent Nutrition 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000000171 quenching effect Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000020183 skimmed milk Nutrition 0.000 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- 150000008163 sugars Chemical class 0.000 description 2
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 2
- 208000010470 Ageusia Diseases 0.000 description 1
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- 102000014171 Milk Proteins Human genes 0.000 description 1
- 108010011756 Milk Proteins Proteins 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 235000019666 ageusia Nutrition 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000013022 formulation composition Substances 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- MOYKHGMNXAOIAT-JGWLITMVSA-N isosorbide dinitrate Chemical compound [O-][N+](=O)O[C@H]1CO[C@@H]2[C@H](O[N+](=O)[O-])CO[C@@H]21 MOYKHGMNXAOIAT-JGWLITMVSA-N 0.000 description 1
- 235000021239 milk protein Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 229940066675 ricinoleate Drugs 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000010583 slow cooling Methods 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 239000000600 sorbitol Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- 150000005691 triesters Chemical class 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
Description
本発明は油中水型乳化油脂組成物の製造法に関
するものである。
さらに詳しくは、本発明は、溶解、半溶解状態
下でも安定な油中水型の乳化状態を保持しうる油
中水型乳化油脂組成物の製造法に関するもので、
本発明の製造法によれば通常不可能とされてきた
液状のマーガリン様組成物を安定に製造しうるも
のである。
製菓・製パン業界は最近の生産規模の拡大、機
械化の進展、省力化の観点から、生産の合理化が
益々要請されるようになつてきている。このよう
なことから、製菓・製パン用の油脂においても従
来のラード、マーガリン、シヨートニングのよう
に製パン性のみを満足させる可塑性固型油脂か
ら、取扱いが簡便で作業性を高め得る可塑性油脂
の流動化、すなわちバルクハンドリング化が強く
要望されてきており、すでに、融解状態で扱うメ
ルテツトシヨートニング、固形脂を含有した状態
で流動性を保有させたフルイドシヨートニング、
水中油型に乳化したクリームタイプの油脂等が開
発されてきている。
しかしながら、メルテツトタイプのシヨートニ
ングは高温で取扱うため製菓・製パン工程での品
温の上昇が起る点と可塑性シヨートニングに比較
してパンの品質がやや劣る点で十分でない。ま
た、フイルドシヨートニングはその製造工程、製
造温度処理条件が煩雑であり、保管条件にしても
流動性と固形脂の分離を防止するために常時撹拌
しなければならず面到な点が多い。また風味の面
からみても水性成分を含まないこれらのシヨート
ニングは出来上つたパンの風味が呈味性の水性成
分を含むマーガリンを使用したものより劣る点は
否めない。また、クリームタイプのパン用油脂は
水性成分を含み風味のよいものが出来るものの細
菌上の安定性が極端に悪く、腐敗、発徴が起りバ
ルクハンドリングの条件下ではそれを防止するこ
とは不可能である。バルクハンドリング用油脂の
このような欠点は流動状の製菓・製パン用油脂が
油中水型の乳化型で得られれば解決されるのであ
るが、従来の油中水型乳化脂は、通常、流動状や
溶解状ではその水相エマルジヨンが急速に擬集
し、合体し、強い撹拌を加えていない限り水相と
油相に分離してしまい、乳蛋白、糖類等の呈味性
水性成分を含む場合は急速に腐敗が進んでしまう
ものであつた。
また、従来よりマーガリン類の水分含有率は日
本農林規格にも定められているように22%以下の
ものが通常であつたが、特定の目的たとえば栄養
学的見地からローカロリーマーガリンとして高い
水分含有率のマーガリンも造られてきていた。
一般にマーガリンは連続相すなわち油相の稠度
がある程度以上高くないと急速に分散相である水
のエマルジヨン粒子が合体し、結果的には水相、
油相の液分離が起つてしまうが、分散相である水
相の比率が相対的に高い高水分マーガリンはこの
傾向が特に強く、その製造時においても不都合な
現象を招きやすい。たとえば、通常、マーガリン
は急冷可塑化を行つて製造するが、その前段階の
水相油相の混合タンクにおける予備乳化段階での
水相、油相の分離とか、急冷可塑化の冷却シリン
ダー内部での分離した水の結晶化によるものと推
定されるが、マーガリン組織のザラツキ、更には
それによる掻取り羽根の磨耗、破損が起りやすい
等の問題がある。また、液体状で取扱う目的、た
とえば、食品原料として他の原料と効果的に混ぜ
合せる場合や、バルクハンドリングを行う場合に
は、乳化の破壊とそれに伴う水相の分離、腐敗等
が起るために応用できないものであつた。更に
は、極く低温で使用する目的の場合には常温では
かなり稠度の低いマーガリンとせざるを得ず、こ
のマーガリンの乳化の安定化も難しいものであつ
た。
このような欠点を解消するものとして、最近、
乳化剤としてポリグリセリン縮合リシノレイン酸
エステルを使用することによつて撹拌を加えなく
ても分離しないマーガリンが得られることが報告
されている。
しかしながら、この方法は常温で液状の油脂に
のみ有効で若干とも固形脂を含んだ場合は、その
製造時に油中水型乳化が破壊され、水相と油相が
分離してしまい、更に常温で液状の油脂でも、低
温で固形脂が析出することが原因と思われるが、
通常の、マーガリンを製造するのに用いる急冷可
塑化装置を使用することによつて油中水型乳化が
破壊されてしまう実用に供せないものであつた。
本発明者らは、かかる問題を解決し、製菓・製
パン用バルクハンドリング油脂として、又液体マ
ーガリン、高水分マーガリンとしてすぐれた物
性、組織を有し、且つ固形脂を含有した場合で
も、通常のマーガリン製造装置を用いた場合で
も、溶解、半溶解状態下でも常に安定な油中水型
乳化油脂組成物を得ることを目的として鋭意検討
した結果、油中水型乳化油脂組成物を製造する際
に、2種の特定の乳化剤を併用することによつ
て、急冷可塑化をはじめとする簡単な製造条件で
容易に、上記目的を達成する油中水型乳化油脂組
成物が得られることを見出し、本発明に到達し
た。
即ち、本発明の油中水型乳化油脂組成物の製造
法は、油脂及び水と乳化剤を含有する油中水型乳
化油脂組成物を製造する際に、乳化剤として、ポ
リグリセリン縮合リシノレイン酸エステルと、ソ
ルビタン不飽和脂肪酸エステル及び/又は
HLB10以上の蔗糖脂肪酸エステルを併用するこ
とを特徴とするものである。
以下本発明の油中水型乳化油脂組成物の製造法
について詳述する。
本発明に用いられる油脂としては、天然の動植
物油脂の他それらにエステル交換、水素添加、分
別等を施した加工油脂があげられるが、本発明を
流動状マーガリンの製造法に応用する場合は常温
で流動状もしくは半流動状の油脂を使用する。
油脂及び水の含有量は目的に応じて決められる
べきであるが、製菓・製パン用途の場合は水に対
する油脂の重量比率を2以上にすることが好まし
く、また高水分マーガリン用途の場合は上記比率
を0.8〜2にすることが好ましい。
本発明に用いられるポリグリセリン縮合リシノ
レイン酸エステルとはポリグリセリンと縮合リシ
ノレイン酸とのエステルであり、通常、グリセリ
ン重合度2〜3のポリグリセリンとリシノール酸
の縮合度3〜5の縮合リシノレイン酸とのモノも
しくはジエステルの混合物が用いられる。
上記ポリグリセリン縮合リシノレイン酸エステ
ルの添加量は通常0.1〜3重量%、好ましくは0.5
〜2重量%である。
また、本発明に用いられるHLB10以上の蔗糖
脂肪酸エステルとは炭素数12〜22個の飽和及び/
又は不飽和の脂肪酸と蔗糖とのモノ−、ジ−、ト
リ−、テトラ−、ペンタエステル等の各種のエス
テルあるいはそれらの混合物であり、これらの中
でHLB10以上のものを使用する。HLBが10未満
である場合には、液体マーガリン、高水分マーガ
リン等の品温を高める等、その稠度を低下せしめ
るような条件下では油中水型乳化を安定化する能
力に欠け不適当である。
上記蔗糖脂肪酸エステルの添加量は目的によつ
てことなるが、通常0.1〜10重量%、好ましくは
0.5〜5重量%である。
また、本発明に用いられるソルビタン不飽和脂
肪酸エステルとは炭素数16〜22個の不飽和脂肪酸
を50%、好ましくは70%以上含有する脂肪酸とソ
ルビタンあるいはソルビタンを主成分とし、ソル
ビトール、ソルバイドを含有する混合物とのモノ
エステル、ジエステルまたはトリエステルあるい
はその他のポリエステルである。
上記ソルビタン不飽和脂肪酸エステルの添加量
は目的によつてことなるが、通常0.1〜10重量%、
好ましくは0.5〜5重量%である。
本発明に用いられる乳化剤は、前記ポリグリセ
リン縮合リシノレイン酸エステルと、前記ソルビ
タン不飽和脂肪酸エステル及び/又は前記
HLB10以上の蔗糖脂肪酸エステルとを必須成分
とするものであり、どちらか一方を欠いては本発
明の目的とする安定性の良い油中水型乳化油脂組
成物を得ることができない。
本発明に係る油中水型乳化油脂組成物には目的
に応じて水相、油相の副成分として乳製品、食
塩、糖類、着香料、呈味剤等を自由に含ませるこ
とも可能である。また更には、重合リン酸塩等の
PH、電荷調整剤を用いることによつて更に安定性
を高めることもできる。
本発明に係る油中水型乳化油脂組成物はたとえ
ば以下のようにして得ることができる。
まず、油脂と乳化剤を常温もしくは加熱下に混
合溶解せしめて均一な油相を調製し、一方水もし
くは目的に応じた副成分を溶解せしめた水相を調
製する。次いで、油相と水相を加熱せずにもしく
は加熱しながら油中水型に混合乳化せしめる。得
られた乳化物を殺菌するかもしくは殺菌せずに、
熱交換機等を用いて冷却もしくは冷却可塑化を行
うか又はそのまま放冷して、本発明に係る油中水
型乳化油脂組成物を得る。
本発明の製造法は、流動状態でも溶解状態でも
長期に乳化状態を安定な油中水型乳化油脂組成物
を安定かつ容易に製造しうるものである。
次に実施例及び比較例によつて本発明をさらに
詳細に説明する。
実施例1〜6及び比較例1〜6
第1表及び第2表に示す配合組成及び冷却方法
によつて油中水型乳化油脂組成物を得た。詳細に
説明すると、まず、油脂と乳化剤を混合槽に入れ
60℃前後に加熱し均一に溶解もしくは分散して油
相を調製した。また脱脂粉乳を含む場合は油相に
脱脂粉乳を加えて均一に分散させた。次に、水を
添加し均一に撹拌を行い油中水型乳化となした。
これを急冷可塑化機を通して急冷可塑化するか、
もしくはそのまま徐冷して油中水型乳化油脂組成
物を得た。
得られた油中水型乳化油脂組成物を25℃及び35
℃に保存し、半溶解時及び溶解時の乳化の安定性
(組織状態、分離状態)を評価した。その結果を
第3表に示す。
第3表に示す結果から明らかなように、本発明
の製造法により得られた油中水型乳化油脂組成物
は、急冷可塑化及び徐冷のいずれの製造条件によ
つても溶解時及び半溶解時の油中水型乳化の安定
性が優れているものであつた。
The present invention relates to a method for producing a water-in-oil emulsified oil and fat composition. More specifically, the present invention relates to a method for producing a water-in-oil emulsified fat composition that can maintain a stable water-in-oil emulsified state even in a dissolved or semi-dissolved state.
According to the production method of the present invention, it is possible to stably produce a liquid margarine-like composition, which has normally been considered impossible. In the confectionery and bread making industries, there has been an increasing demand for rationalization of production due to the recent expansion of production scale, progress in mechanization, and labor saving. For this reason, in the field of oils and fats for confectionery and bread making, there has been a shift from plastic solid fats and fats that only satisfy bread-making properties, such as conventional lard, margarine, and flour toning, to plastic fats and fats that are easier to handle and can improve workability. There is a strong demand for fluidization, that is, bulk handling, and there are already two types of methods: melt shotoning that can be handled in a molten state, fluid shotoning that maintains fluidity while containing solid fat,
Cream-type oils and fats emulsified in an oil-in-water type have been developed. However, melt-type shortening is not sufficient because it is handled at high temperatures, resulting in an increase in product temperature during confectionery and bread-making processes, and the quality of the bread is slightly inferior to that of plastic shortening. In addition, the production process and production temperature treatment conditions for field shortening are complicated, and storage conditions require constant stirring in order to improve fluidity and prevent separation of solid fats, which is problematic. Also, from the point of view of flavor, it cannot be denied that these bread tonings, which do not contain an aqueous component, have a flavor inferior to those made using margarine that contains a flavorful aqueous component. In addition, although cream-type bread fats and oils contain aqueous components and can produce good flavor, they have extremely poor bacterial stability, leading to spoilage and development, which is impossible to prevent under bulk handling conditions. It is. These disadvantages of bulk handling fats and oils can be solved if fluid confectionery and bread making fats and oils can be obtained in the form of water-in-oil emulsions, but conventional water-in-oil emulsions are usually In a fluid or dissolved state, the aqueous phase emulsion rapidly aggregates and coalesces, and unless strong stirring is applied, it separates into an aqueous phase and an oil phase, resulting in the loss of taste-producing aqueous components such as milk proteins and sugars. If this were to occur, corruption would progress rapidly. In addition, the moisture content of margarines has conventionally been 22% or less as stipulated in the Japanese Agricultural Standards, but for specific purposes such as nutritional reasons, low-calorie margarines with high moisture content have been used. Margarine was also produced. Generally, in margarine, unless the consistency of the continuous phase, that is, the oil phase, is higher than a certain level, the water emulsion particles that are the dispersed phase will rapidly coalesce, and as a result, the aqueous phase,
Liquid separation of the oil phase occurs, and this tendency is particularly strong in high-moisture margarine, which has a relatively high proportion of the aqueous phase as the dispersed phase, and is likely to cause undesirable phenomena during its production. For example, margarine is usually produced by rapid plasticization, but the water and oil phases are separated in the pre-emulsification stage in a mixing tank for the water and oil phases, or in the cooling cylinder for rapid plasticization. This is presumed to be due to the crystallization of the separated water, but there are problems such as the roughness of the margarine structure and the resulting abrasion and breakage of the scraping blades. In addition, when handling in liquid form, for example, when effectively mixing it with other raw materials as a food raw material, or when performing bulk handling, the destruction of emulsification and the resulting separation of the aqueous phase, spoilage, etc. may occur. It could not be applied to Furthermore, if the margarine is intended to be used at extremely low temperatures, it is necessary to use margarine that has a considerably low consistency at room temperature, and it is difficult to stabilize the emulsification of this margarine. Recently, as a solution to these shortcomings,
It has been reported that by using polyglycerin condensed ricinoleic acid ester as an emulsifier, margarine that does not separate even without stirring can be obtained. However, this method is only effective for oils and fats that are liquid at room temperature, and if they contain even some solid fat, the water-in-oil emulsion will be destroyed during production, and the water phase and oil phase will separate. The cause seems to be that solid fats precipitate at low temperatures, even in liquid fats and oils.
The water-in-oil emulsion is destroyed by using the ordinary quenching plasticizing equipment used to produce margarine, making it impractical. The present inventors have solved this problem and have found that it has excellent physical properties and structure as a bulk handling fat for confectionery and bread making, liquid margarine, and high moisture margarine, and even when it contains solid fat, it can be used as a bulk handling fat for confectionery and bread making. As a result of intensive studies aimed at obtaining a water-in-oil emulsified oil-fat composition that is always stable even in a dissolved or semi-dissolved state, even when using margarine manufacturing equipment, we found that when manufacturing a water-in-oil emulsified oil-fat composition, It was discovered that by using two specific emulsifiers together, a water-in-oil emulsified fat composition that achieves the above objectives can be easily obtained under simple manufacturing conditions including rapid plasticization. , arrived at the present invention. That is, the method for producing a water-in-oil emulsified oil-fat composition of the present invention includes using a polyglycerin condensed ricinoleic acid ester as an emulsifier when producing a water-in-oil emulsified oil-fat composition containing oil, water, and an emulsifier. , sorbitan unsaturated fatty acid ester and/or
It is characterized by the combined use of a sucrose fatty acid ester with an HLB of 10 or higher. The method for producing the water-in-oil emulsified oil/fat composition of the present invention will be described in detail below. The oils and fats used in the present invention include natural animal and vegetable oils as well as processed oils and fats obtained by subjecting them to transesterification, hydrogenation, fractionation, etc.; Use fluid or semi-liquid fats and oils. The content of oil and water should be determined depending on the purpose, but in the case of confectionery and bread making applications, it is preferable that the weight ratio of oil and fat to water is 2 or more, and in the case of high moisture margarine applications, the above-mentioned Preferably, the ratio is between 0.8 and 2. The polyglycerin condensed ricinoleic acid ester used in the present invention is an ester of polyglycerin and condensed ricinoleic acid, and is usually composed of polyglycerin with a degree of glycerin polymerization of 2 to 3 and condensed ricinoleic acid with a degree of condensation of ricinoleic acid of 3 to 5. Mixtures of mono- or diesters are used. The amount of the polyglycerin condensed ricinoleic acid ester added is usually 0.1 to 3% by weight, preferably 0.5% by weight.
~2% by weight. In addition, the sucrose fatty acid ester with an HLB of 10 or more used in the present invention is a saturated fatty acid ester having 12 to 22 carbon atoms and/or
or various esters such as mono-, di-, tri-, tetra-, and pentaesters of unsaturated fatty acids and sucrose, or mixtures thereof, and among these, those having an HLB of 10 or more are used. If the HLB is less than 10, it is unsuitable because it lacks the ability to stabilize water-in-oil emulsions under conditions that reduce the consistency of liquid margarine, high-moisture margarine, etc., such as by increasing the product temperature. . The amount of the sucrose fatty acid ester added varies depending on the purpose, but is usually 0.1 to 10% by weight, preferably
It is 0.5 to 5% by weight. In addition, the sorbitan unsaturated fatty acid ester used in the present invention is a fatty acid containing 50%, preferably 70% or more, of unsaturated fatty acids having 16 to 22 carbon atoms, and sorbitan or sorbitan as the main components, and contains sorbitol and sorbide. mixtures of monoesters, diesters or triesters or other polyesters. The amount of the sorbitan unsaturated fatty acid ester added varies depending on the purpose, but is usually 0.1 to 10% by weight.
Preferably it is 0.5 to 5% by weight. The emulsifier used in the present invention includes the polyglycerin condensed ricinoleate ester, the sorbitan unsaturated fatty acid ester, and/or the sorbitan unsaturated fatty acid ester.
It contains a sucrose fatty acid ester with an HLB of 10 or more as an essential component, and without either one, it is not possible to obtain a highly stable water-in-oil emulsified fat composition, which is the object of the present invention. Depending on the purpose, the water-in-oil emulsified oil and fat composition of the present invention may contain dairy products, salt, sugars, flavoring agents, flavoring agents, etc. as subcomponents of the aqueous phase and oil phase. be. Furthermore, polymerized phosphates, etc.
Stability can be further improved by using PH and a charge control agent. The water-in-oil emulsified oil and fat composition according to the present invention can be obtained, for example, as follows. First, a homogeneous oil phase is prepared by mixing and dissolving oil and fat and an emulsifier at room temperature or under heating, and on the other hand, an aqueous phase is prepared by dissolving water or a subcomponent depending on the purpose. Next, the oil phase and the water phase are mixed and emulsified into a water-in-oil type without or with heating. Sterilize the obtained emulsion or without sterilizing it,
The water-in-oil emulsified fat composition according to the present invention is obtained by cooling or cooling plasticization using a heat exchanger or the like, or by cooling as is. The production method of the present invention makes it possible to stably and easily produce a water-in-oil emulsified fat composition that maintains a stable emulsified state for a long period of time in either a fluidized state or a dissolved state. Next, the present invention will be explained in more detail with reference to Examples and Comparative Examples. Examples 1 to 6 and Comparative Examples 1 to 6 Water-in-oil emulsified oil and fat compositions were obtained using the formulation compositions and cooling methods shown in Tables 1 and 2. To explain in detail, first, oil and fat and emulsifier are placed in a mixing tank.
An oil phase was prepared by heating to around 60°C to uniformly dissolve or disperse. When skim milk powder was included, skim milk powder was added to the oil phase and uniformly dispersed. Next, water was added and stirred uniformly to form a water-in-oil emulsion.
Either pass this through a quenching plasticizer to quench and plasticize it, or
Alternatively, a water-in-oil type emulsified oil/fat composition was obtained by slowly cooling the mixture as it was. The obtained water-in-oil emulsified oil and fat composition was heated at 25°C and 35°C.
The emulsion was stored at ℃, and the stability of the emulsion (structure state, separation state) during semi-dissolution and dissolution was evaluated. The results are shown in Table 3. As is clear from the results shown in Table 3, the water-in-oil emulsified fat composition obtained by the production method of the present invention can be used both during dissolution and half-time under both the production conditions of rapid plasticization and slow cooling. The stability of the water-in-oil emulsion during dissolution was excellent.
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
【表】【table】
Claims (1)
油脂組成物を製造する際に、乳化剤として、ポリ
グリセリン縮合リシノレイン酸エステルと、ソル
ビタン不飽和脂肪酸エステル及び/又はHLB10
以上の蔗糖脂肪酸エステルを併用することを特徴
とする、油中水型乳化油脂組成物の製造法。1. When producing a water-in-oil emulsified fat composition containing oil, water, and an emulsifier, polyglycerin condensed ricinoleic acid ester, sorbitan unsaturated fatty acid ester, and/or HLB10 are used as emulsifiers.
A method for producing a water-in-oil emulsified oil and fat composition, characterized by using the above sucrose fatty acid esters in combination.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58005459A JPS59130526A (en) | 1983-01-17 | 1983-01-17 | Production of water-in-oil type emulsified fat and oil composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58005459A JPS59130526A (en) | 1983-01-17 | 1983-01-17 | Production of water-in-oil type emulsified fat and oil composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59130526A JPS59130526A (en) | 1984-07-27 |
JPH0347137B2 true JPH0347137B2 (en) | 1991-07-18 |
Family
ID=11611803
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58005459A Granted JPS59130526A (en) | 1983-01-17 | 1983-01-17 | Production of water-in-oil type emulsified fat and oil composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59130526A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60262550A (en) * | 1984-06-08 | 1985-12-25 | Meiji Milk Prod Co Ltd | Production of cream for coffee |
-
1983
- 1983-01-17 JP JP58005459A patent/JPS59130526A/en active Granted
Also Published As
Publication number | Publication date |
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JPS59130526A (en) | 1984-07-27 |
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