JPS6324652B2 - - Google Patents
Info
- Publication number
- JPS6324652B2 JPS6324652B2 JP59130849A JP13084984A JPS6324652B2 JP S6324652 B2 JPS6324652 B2 JP S6324652B2 JP 59130849 A JP59130849 A JP 59130849A JP 13084984 A JP13084984 A JP 13084984A JP S6324652 B2 JPS6324652 B2 JP S6324652B2
- Authority
- JP
- Japan
- Prior art keywords
- edible
- powder
- oils
- fat
- fats
- 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
Links
- 239000003925 fat Substances 0.000 claims description 28
- 239000000203 mixture Substances 0.000 claims description 23
- 239000002775 capsule Substances 0.000 claims description 19
- 235000014633 carbohydrates Nutrition 0.000 claims description 17
- 150000001720 carbohydrates Chemical class 0.000 claims description 17
- 239000008157 edible vegetable oil Substances 0.000 claims description 15
- 239000003921 oil Substances 0.000 claims description 14
- 229920002472 Starch Polymers 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- 235000019698 starch Nutrition 0.000 claims description 7
- 239000008107 starch Substances 0.000 claims description 7
- 229930006000 Sucrose Natural products 0.000 claims description 6
- 239000005720 sucrose Substances 0.000 claims description 6
- 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 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 235000019197 fats Nutrition 0.000 description 26
- 239000000843 powder Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 14
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 13
- 235000019198 oils Nutrition 0.000 description 13
- 235000019441 ethanol Nutrition 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 238000003756 stirring Methods 0.000 description 8
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 7
- 238000001816 cooling Methods 0.000 description 7
- GVJHHUAWPYXKBD-UHFFFAOYSA-N (±)-α-Tocopherol Chemical compound OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 description 6
- 235000014347 soups Nutrition 0.000 description 6
- GUBGYTABKSRVRQ-XLOQQCSPSA-N Alpha-Lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- 239000003995 emulsifying agent Substances 0.000 description 5
- 239000000839 emulsion Substances 0.000 description 5
- 235000013305 food Nutrition 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 235000014593 oils and fats Nutrition 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 229930195727 α-lactose Natural products 0.000 description 4
- 241000234282 Allium Species 0.000 description 3
- 235000002732 Allium cepa var. cepa Nutrition 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 244000203593 Piper nigrum Species 0.000 description 3
- 235000008184 Piper nigrum Nutrition 0.000 description 3
- 229930003427 Vitamin E Natural products 0.000 description 3
- 239000003963 antioxidant agent Substances 0.000 description 3
- 235000006708 antioxidants Nutrition 0.000 description 3
- 235000015278 beef Nutrition 0.000 description 3
- 235000013614 black pepper Nutrition 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- WIGCFUFOHFEKBI-UHFFFAOYSA-N gamma-tocopherol Natural products CC(C)CCCC(C)CCCC(C)CCCC1CCC2C(C)C(O)C(C)C(C)C2O1 WIGCFUFOHFEKBI-UHFFFAOYSA-N 0.000 description 3
- 229940029982 garlic powder Drugs 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- LPUQAYUQRXPFSQ-DFWYDOINSA-M monosodium L-glutamate Chemical compound [Na+].[O-]C(=O)[C@@H](N)CCC(O)=O LPUQAYUQRXPFSQ-DFWYDOINSA-M 0.000 description 3
- 235000013923 monosodium glutamate Nutrition 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000001931 piper nigrum l. white Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 235000019165 vitamin E Nutrition 0.000 description 3
- 229940046009 vitamin E Drugs 0.000 description 3
- 239000011709 vitamin E Substances 0.000 description 3
- JLPULHDHAOZNQI-ZTIMHPMXSA-N 1-hexadecanoyl-2-(9Z,12Z-octadecadienoyl)-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCCCCCC\C=C/C\C=C/CCCCC JLPULHDHAOZNQI-ZTIMHPMXSA-N 0.000 description 2
- NLZUEZXRPGMBCV-UHFFFAOYSA-N Butylhydroxytoluene Chemical compound CC1=CC(C(C)(C)C)=C(O)C(C(C)(C)C)=C1 NLZUEZXRPGMBCV-UHFFFAOYSA-N 0.000 description 2
- 244000000626 Daucus carota Species 0.000 description 2
- 235000002767 Daucus carota Nutrition 0.000 description 2
- 239000001692 EU approved anti-caking agent Substances 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000005280 amorphization Methods 0.000 description 2
- 235000014121 butter Nutrition 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 235000013373 food additive Nutrition 0.000 description 2
- 239000002778 food additive Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 235000021552 granulated sugar Nutrition 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000002020 sage Nutrition 0.000 description 2
- 229940073490 sodium glutamate Drugs 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 229940083466 soybean lecithin Drugs 0.000 description 2
- 239000003549 soybean oil Substances 0.000 description 2
- 235000012424 soybean oil Nutrition 0.000 description 2
- 235000000346 sugar Nutrition 0.000 description 2
- 239000006188 syrup Substances 0.000 description 2
- 235000020357 syrup Nutrition 0.000 description 2
- 235000019640 taste Nutrition 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- URQMEZRQHLCJKR-UHFFFAOYSA-N 3-Methyl-5-propyl-2-cyclohexen-1-one Chemical compound CCCC1CC(C)=CC(=O)C1 URQMEZRQHLCJKR-UHFFFAOYSA-N 0.000 description 1
- 239000004278 EU approved seasoning Substances 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 description 1
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 1
- 244000178231 Rosmarinus officinalis Species 0.000 description 1
- 235000019485 Safflower oil Nutrition 0.000 description 1
- 240000002657 Thymus vulgaris Species 0.000 description 1
- 235000007303 Thymus vulgaris Nutrition 0.000 description 1
- JAZBEHYOTPTENJ-JLNKQSITSA-N all-cis-5,8,11,14,17-icosapentaenoic acid Chemical compound CC\C=C/C\C=C/C\C=C/C\C=C/C\C=C/CCCC(O)=O JAZBEHYOTPTENJ-JLNKQSITSA-N 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 150000008064 anhydrides Chemical class 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000010692 aromatic oil Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 229960005135 eicosapentaenoic acid Drugs 0.000 description 1
- JAZBEHYOTPTENJ-UHFFFAOYSA-N eicosapentaenoic acid Natural products CCC=CCC=CCC=CCC=CCC=CCCCC(O)=O JAZBEHYOTPTENJ-UHFFFAOYSA-N 0.000 description 1
- 235000020673 eicosapentaenoic acid Nutrition 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 235000002864 food coloring agent Nutrition 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000008101 lactose Substances 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 235000013310 margarine Nutrition 0.000 description 1
- 239000003264 margarine Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 235000021243 milk fat Nutrition 0.000 description 1
- 239000004223 monosodium glutamate Substances 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- DOIRQSBPFJWKBE-UHFFFAOYSA-N phthalic acid di-n-butyl ester Natural products CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 1
- 235000015277 pork Nutrition 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000003813 safflower oil Substances 0.000 description 1
- 235000005713 safflower oil Nutrition 0.000 description 1
- 235000020183 skimmed milk Nutrition 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 229940075554 sorbate Drugs 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- -1 sucrose fatty acid esters Chemical class 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
- 239000001585 thymus vulgaris Substances 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
Description
(産業上の利用分野)
本発明は食用油脂含有カプセルの製造法に関す
る。
(従来の技術)
特公昭34−5600号公報及び米国特許第2809895
号明細書
芳香油をコーンシロツプ(水飴)に分散させた
乳濁液を微粒子状の固体とする方法が開示されて
いる。
米国特許第3041180号明細書
上記発明の関連技述であり、コーンシロツプに
グリセロール、グリコール類及び乳化剤を加える
ことにより乳化を容易にした方法が開示されてい
る。
特開昭58−116652号公報
食用固形油脂を粉末調味料に吸着せしめ、顆粒
を得る方法が開示されている。
(発明が解決しようとする問題点)
近年は飲食品に対する嗜好の変化に対応してそ
の形態も様々に変つてきている。そのため、飲食
品の素材である各種の食用油脂類についても粉末
状乃至顆粒状のものが要望されている。
特定の素材を粉末乃至顆粒化する方法として乳
糖などへの吸着法や噴霧乾燥法、顆粒造粒法など
が知られており、食用油脂類についてもこれらの
方法の適用が試みられている。
しかしながら、多大の努力にも拘らず、市販の
粉末油脂はその被覆が不完全であるため、経時的
に油脂特有の酸化による劣化を受け易く、さらに
比較的吸湿性に富むため、保存性に劣り固化し易
い。しかも、溶解性も不十分であり、ママコにな
り易く、その上溶解した状態でも透明性に欠ける
ものが多い等未だ多くの問題点があり、これら欠
点の解消された粉末状乃至顆粒状の食用油脂の出
現が望まれている。
(問題点を解決するための手段)
本発明者らは、上記問題点を解決すべく鋭意研
究を重ねた結果、シヨ糖と或種の澱粉加水分解物
よりなる混合物を用いて食用油脂をカプセル化す
ると、得られるカプセルは細粒であるにも拘ら
ず、外気との接触はほぼ完全に断たれるため、食
用油脂の酸化による劣化も少なく、極めて安定し
た粉末状乃至顆粒状の製品であることを見出し、
かかる知見に基いて本発明を完成したのである。
すなわち本発明は、食用油脂を、DEが5〜12
である澱粉加水分解物と蔗糖の重量混合比が40:
60〜55:45の糖質混合物にてカプセル化すること
を特徴とする食用油脂含有カプセルの製造法を提
供するものである。
本発明に用いられる食用油脂には特別な制限は
なく、例えば大豆油、コーン油、サフラワー油な
どの精製植物性食用油脂、乳脂、牛脂、豚脂など
の精製動物性油脂、これらの加工油脂類、例えば
バター、マーガリンなどを挙げることができる。
次に、糖質混合物の成分である澱粉加水分解物
としてはDEが5〜12の範囲のものを用い、好ま
しくはDE7〜8のものを使用する。DEの大きい
ものはアモルフアス化は良好であるが、吸湿性が
大きくなり、またDEの小さいものは吸湿性は少
なくなるがアモルフアス化が悪くなり、結晶化し
てカプセルが壊れ易くなる。これら糖質の特徴と
して、純粋なものほど一般的に結晶化し易く、ま
たアモルフアス状態にないと製造時にきれいな糸
状で射出されて来ないので、アモルフアスの良否
が製品化に与える影響が非常に大きい。したがつ
て、混合すべき糖質の種類、混合比率等は重要な
要素である。
本発明では蔗糖と澱粉加水分解物を重量混合比
が40:60〜55:45の範囲で混合して得られる糖質
混合物を用いており、その結果最も良好なカプセ
ルを得ることができる。
食用油脂を糖質混合物の溶液に分散させるにあ
たり乳化剤を加えることが望ましい。乳化剤とし
ては食品添加物として許可されたものを任意に使
用できるが、特に大豆レシチン、蔗糖脂肪酸エス
テルであつてHLBが約4〜12のものが好ましい。
乳化剤の添加量は原料食用油脂の重量に基いて3
〜5%程度で十分である。
そのほか必要に応じて酸化防止剤や他の添加物
を適宜添加することができる。酸化防止剤として
は食品添加物として許容されているもの、例えば
l−ソルビン酸ナトリウム、2,6−ジ−t−ブ
チル−4−メチルフエノール(BHT)、ビタミン
Eなどや天然のローズマリー、セージなどの抽出
物等を用いることができ、特に糖質と食用油脂と
の調和の面からビタミンEが好ましい。なお、酸
化防止剤を用いる場合、その添加量は原料食用油
脂の重量に基いて約2%程度が適当である。その
他の添加物としてはフレーバー、食用色素などの
ほかエイコサペンタエン酸等の栄養物質やグルタ
ミン酸ソーダ等の呈味物質などがある。
本発明の食用油脂含有カプセルは以下の方法に
より製造することができる。
まず、蔗糖と澱粉加水分解物の混合物に少量の
水を加えて加熱溶融する。一方、食用油脂には乳
化剤等の補助成分を適宜加え十分に混合する。
前記糖質混合物の加熱を停止した後、激しく撹
拌しながら必要量の食用油脂を徐々に添加、分散
せしめる。ここで糖質混合物に対する食用油脂の
配合量については0.2〜20重量%とすべきであり、
品質の安定性の面から0.5〜10重量%が好ましい。
糖質混合物に食用油脂を添加した後、若干撹拌
を続ける。このようにして得られた乳化物(マト
リツクス)を加温したエクストルーダーに移す。
一方、冷却槽にアルコールを入れ、約−10℃〜−
20℃に冷却しておく。アルコールは冷却と洗浄を
目的として用いられるものであり、食品衛生上害
を与えないものであればよいが、加温された糖質
混合物と接触することを考慮すると、沸点が低す
ぎるものは不適当である。しかし、再利用のため
に蒸留精製することを考慮すると、低沸点のアル
コールが望ましく、また水分は糖質の流出の原因
となるので出来るだけ無水物として蒸留回収ので
きることが好ましい。これらの要求を満足するア
ルコールとしてはイソプロピルアルコールが最も
好ましいが、エチルアルコールも十分に使用する
ことができる。
乳化物(マトリツクス)を撹拌しながらエクス
トルーダーより前記冷却槽に射出する。この間、
冷却槽内の温度上昇を抑制するため十分に冷却し
ておくことが必要であり、射出された粒子が軟化
しないように約10℃以下に保つべきである。射出
終了後も少し撹拌を続け、十分に破砕、冷却、外
表面の洗浄を行なつた後、遠心分離等の操作でカ
プセルとアルコールを分離する。この分離操作は
食用油脂カプセルとアルコールが分離でき、粒子
の破砕を伴なわないものであれば各種の手段を適
用することができる。
アルコール分離後の食用油脂カプセルは再固結
を防止するため、ケーキング防止剤を添加、混和
することが望ましい。ここでケーキング防止剤と
しては種々のものが使用できるが、第3燐酸カル
シウム、α−乳糖などが好ましく、特にα−乳糖
が好適である。ケーキング防止剤の添加量は適宜
決定すればよいが、α−乳糖の場合は糖質混合物
の重量に基いて1〜5%、好ましくは2〜3%が
適当である。
ケーキング防止剤と混和後、食用油脂カプセル
の乾燥を行なう。乾燥は種々の方法により実施し
うるが、未乾燥粒子が熱のために溶解したり、流
動のために粉末化する等の欠点がない方法が適当
である。また、乾燥は可及的に低温で行なうこと
が望ましい。この目的のためには、真空回転乾燥
機にて加熱温度約30〜35℃、真空度約20〜
50Torrにて静かに回転させながら乾燥すること
が好ましい。
(発明の効果)
本発明により得られる食用油脂含有カプセルは
吸湿に対する保存性にすぐれており、溶解性も良
好である。その上、溶液状にて使用する場合、透
明性にすぐれており、広範囲に及ぶ利用が期待で
きる。
(実施例)
次に、実施例および使用例により本発明を詳し
く説明する。
参考例 1
各種のケーキング防止剤についてその性能を下
記の方法により評価した。結果を第1表に示す。
(1) 溶解性
水または1%クエン酸水溶液100mlにケーキ
ング防止剤1gを入れ、撹拌して溶解せしめ、
肉眼にて判定した。
(2) ケーキング防止効果
前記した本発明の方法によりカプセル化した
食用油脂をアルコールと分離した後、未乾燥の
状態にて湿つた重量に対して所定のケーキング
防止剤3重量%を加えた。
次いで、これをロータリーエバポレーター中
で約40℃の湯浴上で減圧下に乾燥した。乾燥
後、約24時間開放下(または室内)に放置した
のちカプセルの外表面の状態を観察し、以下の
如く判定した。
〇……サラサラした状態のもの
△……ややブロツキングを生ずるもの
×……ブロツキングを生ずるもの
(Industrial Application Field) The present invention relates to a method for producing edible oil- and fat-containing capsules. (Prior art) Japanese Patent Publication No. 34-5600 and U.S. Patent No. 2809895
A method is disclosed in which an emulsion in which an aromatic oil is dispersed in corn syrup is made into a finely divided solid. US Patent No. 3,041,180 This is related to the above invention, and discloses a method in which emulsification is facilitated by adding glycerol, glycols, and an emulsifier to corn syrup. JP-A-58-116652 discloses a method for obtaining granules by adsorbing solid edible fats and oils onto powdered seasonings. (Problems to be Solved by the Invention) In recent years, the forms of food and drink have been changing in response to changes in tastes for food and drink. Therefore, there is a demand for various edible oils and fats that are raw materials for food and drink products in powder or granule form. Known methods for powdering or granulating specific materials include lactose adsorption methods, spray drying methods, and granulation methods, and attempts have been made to apply these methods to edible oils and fats as well. However, despite many efforts, commercially available powdered fats and oils have incomplete coatings, so they are susceptible to deterioration over time due to oxidation that is characteristic of fats and oils.Furthermore, they are relatively hygroscopic, resulting in poor shelf life. Easy to solidify. Moreover, there are still many problems such as insufficient solubility, easy to form lumps, and even in the dissolved state, many of them lack transparency. The appearance of fats and oils is desired. (Means for Solving the Problems) As a result of extensive research in order to solve the above problems, the present inventors have found that edible fats and oils are encapsulated using a mixture of sucrose and a certain type of starch hydrolyzate. Although the resulting capsules are fine particles, contact with the outside air is almost completely cut off, so there is little deterioration due to oxidation of edible fats and oils, and the product is extremely stable in the form of powder or granules. I found out that
The present invention was completed based on this knowledge. That is, the present invention uses edible fats and oils with a DE of 5 to 12.
The weight mixing ratio of starch hydrolyzate and sucrose is 40:
The present invention provides a method for producing edible fat-containing capsules, which is characterized in that the capsules are encapsulated with a carbohydrate mixture of 60 to 55:45. The edible oils and fats used in the present invention are not particularly limited, and include, for example, refined vegetable edible oils such as soybean oil, corn oil, and safflower oil, refined animal fats and oils such as milk fat, beef tallow, and pork fat, and processed oils and fats thereof. Examples include butter, margarine, etc. Next, as the starch hydrolyzate which is a component of the carbohydrate mixture, one having a DE of 5 to 12 is used, preferably one having a DE of 7 to 8. Those with a high DE have good amorphization, but have high hygroscopicity, and those with a low DE have low hygroscopicity, but have poor amorphization, making it easy to crystallize and break the capsule. Characteristics of these carbohydrates are that the purer they are, the easier they are to crystallize, and if they are not in an amorphous state, they will not be injected in the form of clean threads during production, so the quality of the amorphous has a very large effect on the commercialization of the product. Therefore, the types of carbohydrates to be mixed, the mixing ratio, etc. are important factors. In the present invention, a carbohydrate mixture obtained by mixing sucrose and starch hydrolyzate at a weight mixing ratio of 40:60 to 55:45 is used, and as a result, the best capsules can be obtained. It is desirable to add an emulsifier when dispersing the edible fat into the carbohydrate mixture solution. Any emulsifier that is approved as a food additive can be used, but soybean lecithin and sucrose fatty acid esters having an HLB of about 4 to 12 are particularly preferred.
The amount of emulsifier added is 3 based on the weight of the raw edible fat.
~5% is sufficient. In addition, antioxidants and other additives may be added as appropriate. Antioxidants include those permitted as food additives, such as sodium l-sorbate, 2,6-di-t-butyl-4-methylphenol (BHT), vitamin E, natural rosemary, and sage. Vitamin E is particularly preferred from the viewpoint of harmony between carbohydrates and edible fats and oils. In addition, when using an antioxidant, the appropriate amount of addition is about 2% based on the weight of the raw material edible fat. Other additives include flavors, food colors, and other nutritional substances such as eicosapentaenoic acid and taste substances such as monosodium glutamate. The edible fat-containing capsule of the present invention can be produced by the following method. First, a small amount of water is added to a mixture of sucrose and starch hydrolyzate and the mixture is heated and melted. On the other hand, auxiliary components such as emulsifiers are appropriately added to the edible oil and fat and mixed thoroughly. After stopping the heating of the carbohydrate mixture, a required amount of edible oil and fat is gradually added and dispersed while stirring vigorously. Here, the amount of edible oil and fat added to the carbohydrate mixture should be 0.2 to 20% by weight.
From the viewpoint of quality stability, 0.5 to 10% by weight is preferable. After adding the edible fat and oil to the carbohydrate mixture, continue stirring slightly. The emulsion (matrix) thus obtained is transferred to a heated extruder.
Meanwhile, put alcohol in a cooling tank and
Cool to 20℃. Alcohol is used for cooling and cleaning purposes, so long as it does not pose a food hygiene hazard, alcohol is fine, but alcohol with a boiling point that is too low should not be used, considering that it will come into contact with the heated carbohydrate mixture. Appropriate. However, in consideration of distillation and purification for reuse, it is desirable to use an alcohol with a low boiling point, and since water causes the outflow of carbohydrates, it is preferable that the alcohol can be distilled and recovered as an anhydride as much as possible. Isopropyl alcohol is the most preferred alcohol that satisfies these requirements, but ethyl alcohol can also be used satisfactorily. The emulsion (matrix) is injected into the cooling tank from the extruder while stirring. During this time,
Sufficient cooling is necessary to suppress the temperature rise in the cooling tank, and the temperature should be kept below about 10°C to prevent the injected particles from softening. After the injection is completed, stirring is continued for a while to thoroughly crush, cool, and wash the outer surface, and then the capsules and alcohol are separated by centrifugation or other operations. Various means can be used for this separation operation as long as the edible fat capsule and the alcohol can be separated and the separation does not involve crushing the particles. In order to prevent re-solidification of the edible oil/fat capsules after alcohol separation, it is desirable to add and mix an anti-caking agent. Various anti-caking agents can be used here, but tertiary calcium phosphate, α-lactose and the like are preferred, with α-lactose being particularly preferred. The amount of the anti-caking agent to be added may be determined as appropriate, but in the case of α-lactose, an appropriate amount is 1 to 5%, preferably 2 to 3%, based on the weight of the carbohydrate mixture. After mixing with the anti-caking agent, the edible oil/fat capsules are dried. Drying can be carried out by various methods, but a method that does not have disadvantages such as melting of undried particles due to heat or pulverization due to flowability is suitable. Further, it is desirable that the drying be performed at as low a temperature as possible. For this purpose, use a vacuum rotary dryer at a heating temperature of approximately 30-35℃ and a vacuum degree of approximately 20-35℃.
It is preferable to dry while rotating gently at 50 Torr. (Effects of the Invention) The edible oil-containing capsules obtained by the present invention have excellent preservability against moisture absorption and good solubility. Moreover, when used in the form of a solution, it has excellent transparency and can be expected to be used over a wide range of areas. (Example) Next, the present invention will be explained in detail with reference to Examples and Usage Examples. Reference Example 1 The performance of various anti-caking agents was evaluated by the following method. The results are shown in Table 1. (1) Solubility Add 1 g of anti-caking agent to 100 ml of water or 1% citric acid aqueous solution, stir to dissolve,
Judgment was made with the naked eye. (2) Anti-caking effect After separating the edible fats and oils encapsulated by the method of the present invention from alcohol, 3% by weight of a predetermined anti-caking agent was added to the wet weight of the oil in an undried state. This was then dried under reduced pressure in a rotary evaporator over a water bath at about 40°C. After drying, the capsule was left in the open (or indoors) for about 24 hours, and then the condition of the outer surface of the capsule was observed and judged as follows. 〇...Smooth condition△...Those that cause some blotching ×...Those that cause blotching
【表】
参考例 2
各種の糖質混合物についてその性能を下記の方
法により評価した。結果を第2表に示す。
(1) 混和状態、アモルフアス構成要素及び射出状
態混合物を肉眼で観察し、以下の如く判定し
た。
◎……良好、〇……やや良、×……不良
(2) 耐吸湿性
20メツシユ(篩上)グラニユー糖20g中に20
メツシユ(篩上)の試料1gを混和し、RH80
%、25℃の恒温恒湿器内に1時間放置した後、
下記の如く判定した。
〇……サラサラした状態のもの
×……一部ブロツキングを起しているもの
××……ほとんどブロツキングを起しているも
の[Table] Reference Example 2 The performance of various carbohydrate mixtures was evaluated by the following method. The results are shown in Table 2. (1) The mixture state, amorphous component, and injection state were observed with the naked eye and judged as follows. ◎...Good, 〇...Slightly good, ×...Poor (2) Moisture absorption resistance 20 mesh (on sieve) 20 g of granulated sugar
Mix 1 g of the mesh sample (on the sieve) and
%, after leaving it in a constant temperature and humidity chamber at 25℃ for 1 hour,
It was determined as follows. 〇……Things that are in a smooth condition×……Those with some blotching ××……Those with mostly blotching
【表】
* 焦結
実施例 1
煮詰釜内に水3を入れ沸騰させた。これに精
製グラニユー糖11Kgと澱粉加水分解物(「パイン
デツクス#1(DE7〜8)」、松谷化学工業(株)製)
9Kgを加えて加熱溶解せしめ、さらに内温117〜
120℃に達するまで煮詰めた。
一方、精製ヘツド1Kgを加温溶解し、これに大
豆レシチン40g、ビタミンE(「イーミツクス−
80」、エーザイ(株)製)20g及びバターフレーバー
(高砂香料工業(株)製)20gを加え、撹拌混合して
溶解せしめ、液状食用油脂を調製した。
前記糖質混合液は加熱を停止し、高速撹拌(約
2000rpm)しながら液状食用油脂を徐々に添加し
た。添加終了後、約1〜2分間撹拌を続け十分に
分散、乳化せしめた。
この乳化液を加温したエクストルーダーに移し
た。また、破砕用撹拌機付の冷却槽に約50のイ
ソプロパノールを入れ約−10℃に冷却しておく。
このイソプロパノールを冷却、撹拌をしながらエ
クストルーダーの押し出し口径0.7mmφの孔より
約2Kg/cm2Gの圧力で前記乳化液を押出した。押
出し終了後の液温は約2℃であつた。
次いで、遠心分離機を用いてアルコールを分離
して得た食用油脂含有カプセルを予めα−乳糖
600gを入れてある真空回転乾燥機へ仕込み、加
熱温度30〜35℃、真空度20〜30Torrで約5時間
乾燥し、製品18.8Kgを得た。本カプセルは乳白
色、ほとんど無臭に近い微粒状粒体であり、20〜
60メツシユのもの13.2Kgであつた。
実施例 2〜6
第3表に示した各成分を所定の割合で使用し、
実施例1と同様にして食用油脂含有カプセルを得
た。
各カプセルの色調は実施例2(乳白色)、実施例
3(褐色)、実施例4(黄色)、実施例5(淡黄色)、
実施例6(乳白色)であつた。[Table] * Scorching Example 1 Water 3 was placed in a boiling pot and brought to a boil. Add to this 11 kg of purified granulated sugar and starch hydrolyzate ("Pinedex #1 (DE7-8)", manufactured by Matsutani Chemical Industry Co., Ltd.)
Add 9 kg and heat to dissolve, further increasing the internal temperature to 117 ~
It was boiled down until it reached 120℃. On the other hand, heat and dissolve 1 kg of purified head, add 40 g of soybean lecithin, and vitamin E ("Emix").
80 (manufactured by Eisai Co., Ltd.) and 20 g of Butter Flavor (manufactured by Takasago International Corporation) were added and stirred and mixed to dissolve, thereby preparing a liquid edible fat. Stop heating the carbohydrate mixture and stir at high speed (approx.
2000 rpm), liquid edible oil and fat were gradually added. After the addition was completed, stirring was continued for about 1 to 2 minutes to sufficiently disperse and emulsify. This emulsion was transferred to a heated extruder. In addition, about 50 g of isopropanol is placed in a cooling tank equipped with a crushing stirrer and cooled to about -10°C.
While cooling and stirring the isopropanol, the emulsion was extruded through a hole having an extrusion diameter of 0.7 mm in an extruder at a pressure of about 2 kg/cm 2 G. The liquid temperature after extrusion was about 2°C. Next, the edible oil-containing capsules obtained by separating alcohol using a centrifuge are pre-mixed with α-lactose.
600 g of the product was placed in a vacuum rotary dryer and dried at a heating temperature of 30 to 35°C and a vacuum of 20 to 30 Torr for about 5 hours to obtain 18.8 kg of product. This capsule is a milky white, almost odorless, fine granular substance with a
The weight of 60 pieces was 13.2 kg. Examples 2 to 6 Each component shown in Table 3 was used in a predetermined ratio,
Edible oil-containing capsules were obtained in the same manner as in Example 1. The color tone of each capsule is Example 2 (milky white), Example 3 (brown), Example 4 (yellow), Example 5 (light yellow),
Example 6 (milky white).
【表】
使用例 1
コンソメスープ粉末
食 塩 70g
砂 糖 16
リンゴ酸 0.3
オニオン末 1
セロリ末 0.2
ガーリツク末 0.2
ホワイトペツパー末 0.4
粉末正油 1.2
実施例1の製品 10.7
上記処方の粉末スープ3gを湯100mlに添加し
たところ、速やかに溶解し、濁りも生じなかつ
た。
使用例 2
粉末ビーフスープ
食 塩 42.7g
グルタミン酸ソーダ 10
キヤロツト末 1.5
オニオン末 2.6
ガーリツク末 0.3
ホワイトペツパー末 0.5
セージ末 0.03
タイム末 0.03
実施例2の製品 12.34
上記処方の粉末スープ2.5gを湯100mlに添加し
たところ、速やかに溶解し、濁りも生じなかつ
た。
使用例 3
粉末中華スープ
ビーフエキスパウダー 3.5g
ゼラチン 0.2
食 塩 19.0
ホワイトペツパー末 0.5
オニオン末 1.0
キヤロツト末 0.3
ガーリツク末 0.2
グルタミン酸ソーダ 2.8
実施例3の製品 12.5
上記処方の粉末スープ4.0gを湯100mlに添加し
たところ、速やかに溶解し、濁りも生ぜず、適度
の油が浮いた。
使用例 4
ケーキミツクス
小麦粉 100重量部
粉 糖 40
脱脂粉乳 10
ベーキングパウダー 3
実施例6の製品 5
食 塩 0.2
上記処方にしたがい各成分を混合してケーキミ
ツクスを作つた。これを約同量の水でといてフラ
イパンにて焼きあげ、チーズ風味のホツトケーキ
を得た。[Table] Usage example 1 Consomme soup powder Salt 70g Sugar 16 Malic acid 0.3 Onion powder 1 Celery powder 0.2 Garlic powder 0.2 White pepper powder 0.4 Powdered soybean oil 1.2 Product of Example 1 10.7 Add 3g of powdered soup of the above formulation to hot water When added to 100 ml, it dissolved quickly and did not become cloudy. Usage example 2 Powdered beef soup Salt 42.7g Sodium glutamate 10 Carrot powder 1.5 Onion powder 2.6 Garlic powder 0.3 White pepper powder 0.5 Sage powder 0.03 Thyme powder 0.03 Product of Example 2 12.34 Add 2.5g of powdered soup of the above recipe to 100ml of hot water. When added, it quickly dissolved and did not become cloudy. Usage example 3 Powdered Chinese soup beef extract powder 3.5g Gelatin 0.2 Salt 19.0 White pepper powder 0.5 Onion powder 1.0 Carrot powder 0.3 Garlic powder 0.2 Sodium glutamate 2.8 Product of Example 3 12.5 Add 4.0g of powdered soup of the above formulation to 100ml of hot water As a result, it dissolved quickly, did not become cloudy, and a moderate amount of oil floated on top. Usage Example 4 Cake Mix Flour 100 parts by weight Powder Sugar 40 Skimmed Milk Powder 10 Baking Powder 3 Product of Example 6 5 Salt 0.2 Cake mix was prepared by mixing each component according to the above recipe. This was mixed with about the same amount of water and baked in a frying pan to obtain a cheese-flavored hot cake.
Claims (1)
解物と蔗糖の重量混合比が40:60〜55:45の糖質
混合物にてカプセル化することを特徴とする食用
油脂含有カプセルの製造法。 2 糖質混合物に対する食用油脂の配合量が0.2
〜20重量%である特許請求の範囲第1項記載の製
造法。[Claims] 1. Edible fats and oils are encapsulated in a carbohydrate mixture of starch hydrolyzate with a DE of 5 to 12 and sucrose in a weight mixing ratio of 40:60 to 55:45. Method for producing edible oil-containing capsules. 2 The amount of edible oil and fat added to the carbohydrate mixture is 0.2
20% by weight of the manufacturing method according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59130849A JPS6112248A (en) | 1984-06-27 | 1984-06-27 | Production of capsule containing edible fat or oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59130849A JPS6112248A (en) | 1984-06-27 | 1984-06-27 | Production of capsule containing edible fat or oil |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6112248A JPS6112248A (en) | 1986-01-20 |
JPS6324652B2 true JPS6324652B2 (en) | 1988-05-21 |
Family
ID=15044126
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59130849A Granted JPS6112248A (en) | 1984-06-27 | 1984-06-27 | Production of capsule containing edible fat or oil |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6112248A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2016049105A (en) * | 2014-08-29 | 2016-04-11 | 花王株式会社 | Method for producing solid dispersion containing difficult-to-dissolve polyphenol |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5011532A (en) * | 1988-03-18 | 1991-04-30 | Fuisz Pharmaceutical Ltd. | Dispersed systems and method of manufacture |
US5709895A (en) * | 1994-05-31 | 1998-01-20 | Takasago International Corporation Usa | Process for producing flavor-containing capsule |
JP2007254339A (en) | 2006-03-22 | 2007-10-04 | Takasago Internatl Corp | Lock-in type powder |
CN113768005B (en) * | 2021-09-13 | 2022-12-20 | 吉林大学 | Macadamia nut tea and preparation method thereof |
-
1984
- 1984-06-27 JP JP59130849A patent/JPS6112248A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2016049105A (en) * | 2014-08-29 | 2016-04-11 | 花王株式会社 | Method for producing solid dispersion containing difficult-to-dissolve polyphenol |
US10894058B2 (en) | 2014-08-29 | 2021-01-19 | Kao Corporation | Method for producing solid dispersion containing hardly soluble polyphenol |
Also Published As
Publication number | Publication date |
---|---|
JPS6112248A (en) | 1986-01-20 |
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