JPH0358704B2 - - Google Patents
Info
- Publication number
- JPH0358704B2 JPH0358704B2 JP59025597A JP2559784A JPH0358704B2 JP H0358704 B2 JPH0358704 B2 JP H0358704B2 JP 59025597 A JP59025597 A JP 59025597A JP 2559784 A JP2559784 A JP 2559784A JP H0358704 B2 JPH0358704 B2 JP H0358704B2
- Authority
- JP
- Japan
- Prior art keywords
- oil
- germ
- enzyme
- added
- treatment
- 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
- 102000004190 Enzymes Human genes 0.000 claims description 26
- 108090000790 Enzymes Proteins 0.000 claims description 26
- 239000000843 powder Substances 0.000 claims description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 235000013339 cereals Nutrition 0.000 claims description 14
- 108091005804 Peptidases Proteins 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 11
- 239000004365 Protease Substances 0.000 claims description 10
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 claims description 10
- 229920002472 Starch Polymers 0.000 claims description 10
- 235000019698 starch Nutrition 0.000 claims description 10
- 239000008107 starch Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 9
- 102000004157 Hydrolases Human genes 0.000 claims description 8
- 108090000604 Hydrolases Proteins 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 5
- 206010042674 Swelling Diseases 0.000 claims description 4
- 210000001161 mammalian embryo Anatomy 0.000 claims description 4
- 230000008961 swelling Effects 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 2
- 239000003921 oil Substances 0.000 description 27
- 235000019198 oils Nutrition 0.000 description 27
- 229940088598 enzyme Drugs 0.000 description 24
- 239000003925 fat Substances 0.000 description 15
- 239000003795 chemical substances by application Substances 0.000 description 11
- 235000019197 fats Nutrition 0.000 description 11
- 238000003756 stirring Methods 0.000 description 8
- 230000001804 emulsifying effect Effects 0.000 description 7
- 239000007921 spray Substances 0.000 description 7
- 241000209140 Triticum Species 0.000 description 6
- 235000021307 Triticum Nutrition 0.000 description 6
- 102000004139 alpha-Amylases Human genes 0.000 description 6
- 108090000637 alpha-Amylases Proteins 0.000 description 6
- 229940024171 alpha-amylase Drugs 0.000 description 6
- 244000052616 bacterial pathogen Species 0.000 description 5
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 5
- 239000010497 wheat germ oil Substances 0.000 description 5
- 239000000839 emulsion Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 108010073178 Glucan 1,4-alpha-Glucosidase Proteins 0.000 description 3
- 102100022624 Glucoamylase Human genes 0.000 description 3
- 240000008042 Zea mays Species 0.000 description 3
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 3
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 3
- 235000005822 corn Nutrition 0.000 description 3
- 235000016709 nutrition Nutrition 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- GHOKWGTUZJEAQD-ZETCQYMHSA-N (D)-(+)-Pantothenic acid Chemical compound OCC(C)(C)[C@@H](O)C(=O)NCCC(O)=O GHOKWGTUZJEAQD-ZETCQYMHSA-N 0.000 description 2
- PVNIIMVLHYAWGP-UHFFFAOYSA-N Niacin Chemical compound OC(=O)C1=CC=CN=C1 PVNIIMVLHYAWGP-UHFFFAOYSA-N 0.000 description 2
- 102000035195 Peptidases Human genes 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 235000020138 yakult Nutrition 0.000 description 2
- OYHQOLUKZRVURQ-NTGFUMLPSA-N (9Z,12Z)-9,10,12,13-tetratritiooctadeca-9,12-dienoic acid Chemical compound C(CCCCCCC\C(=C(/C\C(=C(/CCCCC)\[3H])\[3H])\[3H])\[3H])(=O)O OYHQOLUKZRVURQ-NTGFUMLPSA-N 0.000 description 1
- YLZOPXRUQYQQID-UHFFFAOYSA-N 3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)-1-[4-[2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidin-5-yl]piperazin-1-yl]propan-1-one Chemical compound N1N=NC=2CN(CCC=21)CCC(=O)N1CCN(CC1)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F YLZOPXRUQYQQID-UHFFFAOYSA-N 0.000 description 1
- 108010084185 Cellulases Proteins 0.000 description 1
- 102000005575 Cellulases Human genes 0.000 description 1
- GHOKWGTUZJEAQD-UHFFFAOYSA-N Chick antidermatitis factor Natural products OCC(C)(C)C(O)C(=O)NCCC(O)=O GHOKWGTUZJEAQD-UHFFFAOYSA-N 0.000 description 1
- 102000004882 Lipase Human genes 0.000 description 1
- 108090001060 Lipase Proteins 0.000 description 1
- 239000004367 Lipase Substances 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 235000019485 Safflower oil Nutrition 0.000 description 1
- 241001125046 Sardina pilchardus Species 0.000 description 1
- 235000019486 Sunflower oil Nutrition 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 235000019658 bitter taste Nutrition 0.000 description 1
- 235000021329 brown rice Nutrition 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 235000004626 essential fatty acids Nutrition 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000021323 fish oil Nutrition 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 235000019421 lipase Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229960003512 nicotinic acid Drugs 0.000 description 1
- 235000001968 nicotinic acid Nutrition 0.000 description 1
- 239000011664 nicotinic acid Substances 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- 229940055726 pantothenic acid Drugs 0.000 description 1
- 235000019161 pantothenic acid Nutrition 0.000 description 1
- 239000011713 pantothenic acid Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012254 powdered material Substances 0.000 description 1
- 229940024999 proteolytic enzymes for treatment of wounds and ulcers Drugs 0.000 description 1
- 235000012437 puffed product Nutrition 0.000 description 1
- 230000001007 puffing effect Effects 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 235000005713 safflower oil Nutrition 0.000 description 1
- 239000003813 safflower oil Substances 0.000 description 1
- 235000019512 sardine Nutrition 0.000 description 1
- 239000002600 sunflower oil Substances 0.000 description 1
- 235000019640 taste Nutrition 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 235000019156 vitamin B Nutrition 0.000 description 1
- 239000011720 vitamin B Substances 0.000 description 1
- -1 vitamins B 1 Natural products 0.000 description 1
Landscapes
- Grain Derivatives (AREA)
- Edible Oils And Fats (AREA)
Description
【発明の詳細な説明】
本発明は新規な油脂含有胚芽成分粉末の製造
法、更に詳細には、水に対する乳化性が良好な栄
養価の高い胚芽成分粉末の製造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel method for producing an oil-containing germ component powder, and more particularly to a method for producing a highly nutritious germ component powder that has good emulsifying properties in water.
穀類胚芽は良質の蛋白質、ヒトの体内では合成
されない必須脂肪酸であるリノール酸、ニコチン
酸、パントテン酸、ビタミンB1,B2,B6,E等
の各種ビタミン類、K,Na,Ca,Mg等のミネ
ラル類を豊富に含有し、極めて栄養価値の高いも
のである。従つて、現在、小麦胚芽、玄米胚芽等
の穀類胚芽の粉末、破砕片、フレークが食品とし
て供されているが、これらは味覚、食感の点で食
用適性が悪く、また胚芽中に含まれている油性成
分のためにべたついて粉末化が困難であり、更に
水に対する分散性が悪いという欠点があり、その
利用範囲は著しく制限されていた。 Cereal germ contains high-quality protein, essential fatty acids such as linoleic acid, nicotinic acid, and pantothenic acid that are not synthesized in the human body, various vitamins such as vitamins B 1 , B 2 , B 6 , and E, K, Na, Ca, and Mg. It contains abundant minerals such as, and has extremely high nutritional value. Therefore, currently, powdered, crushed pieces, and flakes of grain germs such as wheat germ and brown rice germ are provided as foods, but these have poor edibility in terms of taste and texture, and the amount of grains contained in the germ is not suitable for eating. Due to the oily component contained therein, it is sticky and difficult to powder, and furthermore, it has the disadvantage of poor dispersibility in water, and its range of use has been severely limited.
斯かる実情から、近年、穀類胚芽の上記有用成
分を抽出し、食用に供せんとする研究が行われて
おり、例えば穀類胚芽を殿粉加水分解酵素の存
在下70℃以上の温度で熱水抽出する方法(特公昭
55−1027号)、加水した穀類胚芽に先ずプロテ
アーゼと麺製複合酵素を作用させ、次いでその処
理物にα−アミラーゼを作用させて抽出する方法
(特開昭48−1170号)が知られている。 Under these circumstances, in recent years, research has been carried out to extract the above-mentioned useful components from grain germ and use it for human consumption. How to extract (Tokukosho
55-1027), a method is known in which hydrated grain germ is first treated with protease and a noodle-making complex enzyme, and then the treated product is treated with α-amylase for extraction (Japanese Patent Application Laid-open No. 1170/1982). There is.
しかしながら、これらの方法で抽出されるもの
は水溶性成分のみであり、油溶性成分は殆んど抽
出されないため、斯くして得られる胚芽エキスは
油溶性成分が不足し、栄養価値が低下することを
免れなかつた。 However, these methods extract only water-soluble components and almost no oil-soluble components, so the germ extract obtained in this way lacks oil-soluble components and has a reduced nutritional value. I couldn't escape it.
そこで、本発明者は、斯かる欠点を克服せんと
種々研究を行い、上記の如くして製した胚芽エキ
スは優れた乳化力を示し、このものに油脂を添加
してこれを乾燥すると、油脂の存在にもかかわら
ず、容易に粉末となり、しかもこの粉末は水に対
する乳化性が高いことを見出した。更にまた、驚
くべきことに、穀類胚芽を酵素処理したものは、
固液分離せずにこれに油脂を加えて乾燥した場合
でも、粉末化が容易であり、しかも水によく乳化
することを見出した。 Therefore, the present inventor conducted various studies to overcome such drawbacks, and found that the germ extract produced as described above showed excellent emulsifying power, and when oil and fat were added to this and dried, oil and fat It was found that the powder was easily powdered despite the presence of , and that this powder had a high emulsifying property in water. Furthermore, surprisingly, enzyme-treated grain germs
It has been found that even when fats and oils are added to this and dried without solid-liquid separation, it can be easily powdered and emulsified well in water.
本発明は、斯かる新知見に基いて完成されたも
ので、穀類胚芽に水の存在下、殿粉加水分解酵素
又は殿粉加水分解酵素と蛋白分解酵素を作用せし
め、次いでこれを加熱処理して得られる酵素処理
物、または該酵素処理物を固液分離して得られる
胚芽エキスに油脂を加えて乾燥することを特徴と
する油脂含有胚芽成分粉末の製造法を提供するも
のである。 The present invention was completed based on this new knowledge, and consists of allowing starch hydrolase or starch hydrolase and proteolytic enzyme to act on grain germ in the presence of water, and then heat-treating the germ. The present invention provides a method for producing an oil-containing germ component powder, which is characterized in that oil is added to an enzyme-treated product obtained by the process, or to an embryo extract obtained by solid-liquid separation of the enzyme-treated product, and then dried.
本発明方法において、穀類胚芽としては、麦
類、米類、とうもろこし等を挙げることができ、
これらは全脂又は脱脂の何れのものでもよく、ま
た粉末、粗砕物、圧扁物の何れの形状のものも使
用できる。 In the method of the present invention, grain germs include wheat, rice, corn, etc.
These may be either full-fat or defatted, and may be in the form of powder, pulverized material, or pressed material.
本発明を実施するには、先ずこれらの穀類胚芽
を酵素処理する。穀類胚芽はそのまま酵素処理に
付すこともできるが、予め膨化処理を行つたもの
は、油溶性成分が多く抽出されると共に収率が高
く好ましい。膨化処理は、穀類胚芽をエクストル
ーダーに供給して、圧力10〜100Kg/cm2、品温60
〜150℃、処理時間10〜120秒で低圧下に放出する
方法、あるいは加熱高圧缶で処理した後急激に低
圧下に放出する方法等によつて行われる。 To carry out the present invention, these grain germs are first treated with enzymes. Cereal germs can be subjected to enzyme treatment as they are, but those that have been previously subjected to a swelling treatment are preferable because many oil-soluble components can be extracted and the yield is high. In the puffing process, grain germ is fed to an extruder at a pressure of 10 to 100 kg/cm 2 and a product temperature of 60°C.
This is carried out by a method in which the material is discharged under low pressure at ~150°C for a treatment time of 10 to 120 seconds, or by a method in which it is treated in a heated high-pressure can and then rapidly discharged under low pressure.
酵素処理を行うには、穀類胚芽に先ず水を加え
る。加水量は、胚芽1重量部(以下単に部と表現
する)に対し水3〜9部になるようにするのが好
ましい。 To carry out the enzyme treatment, water is first added to the grain germ. The amount of water added is preferably 3 to 9 parts by weight of the germ (hereinafter simply expressed as parts).
次いで、加水された胚芽に酵素を作用させる。
酵素としてはα−アミラーゼ剤等の殿粉加水分解
酵素;プロテアーゼ剤等の蛋白分解酵素が使用さ
れる。酵素処理は、殿粉加水分解酵素単独の処理
でも、また殿粉加水分解酵素と蛋白分解酵素処理
を組合せて行うこともできる。就中、殿粉加水分
解酵素処理次いで蛋白分解酵素処理を行うのが最
も好ましい。 Next, enzymes are allowed to act on the hydrated germ.
As the enzyme, starch hydrolyzing enzymes such as α-amylase agents; proteolytic enzymes such as protease agents are used. Enzyme treatment can be carried out using starch hydrolase alone or in combination with starch hydrolase and protease. Among these, it is most preferable to perform starch hydrolase treatment followed by protease treatment.
殿粉加水分解酵素の添加量は、力価として胚芽
1gに対し100〜1000Uが好ましい。該酵素処理
は70〜95℃、好ましくは80〜95℃の温度で行われ
る。尚この際、セルラーゼ類を併用して行うこと
ができ、この場合、溶液の粘度が低下し過性が
よくなり、収率を向上させることができる。蛋白
分解酵素の添加量は、力価として胚芽1gに対し
50〜500Uが好ましく、処理温度は45〜55℃が好
ましく、処理時間は2〜5時間が好ましい。処理
時間がこれより短いと収率が低下し、またこれを
超えると製品に苦味を生ずるので好ましくない。
また、この蛋白分解酵素にグルコアミラーゼ、リ
パーゼ等を併用することができ、かくするときは
胚芽中の殿粉が分解されて製品に甘味と良好なフ
レーバーが付与される。 The amount of starch hydrolase added is preferably 100 to 1000 U per gram of germ in terms of titer. The enzyme treatment is carried out at a temperature of 70-95°C, preferably 80-95°C. At this time, cellulases can be used in combination, and in this case, the viscosity of the solution is reduced and the permeability is improved, so that the yield can be improved. The amount of protease added is based on the titer per 1g of embryo.
The treatment temperature is preferably 50 to 500 U, the treatment temperature is preferably 45 to 55°C, and the treatment time is preferably 2 to 5 hours. If the treatment time is shorter than this, the yield will decrease, and if it exceeds this, the product will have a bitter taste, which is not preferable.
In addition, glucoamylase, lipase, etc. can be used in combination with this protease, and when this is done, the starch in the germ is decomposed and sweetness and good flavor are imparted to the product.
以上のようにして酵素処理したものは、80〜
120℃で10〜30分間加熱処理して酵素の失活と殺
菌を行う。このようにして得られる酵素処理物に
はそのまま油脂を加えることができるが、更に固
液分離して胚芽エキスを分離取得して、これに油
脂を加えることもできる。固液分離は常法によつ
て行うことができ、例えば遠心分離、過等によ
つて行われる。更にまた、固液分離された固形分
は胚芽エキスと混合して本発明方法に使用するこ
とができる。 The enzyme-treated product as described above is 80~
Heat treatment is performed at 120°C for 10 to 30 minutes to inactivate the enzyme and sterilize it. Although fats and oils can be directly added to the enzyme-treated product thus obtained, it is also possible to perform solid-liquid separation to separate and obtain an germ extract, and then add fats and oils to this. Solid-liquid separation can be performed by a conventional method, for example, by centrifugation, filtration, or the like. Furthermore, the solid content separated from solid and liquid can be mixed with germ extract and used in the method of the present invention.
酵素処理物又は胚芽エキスに添加される油脂と
しては、全脂胚芽よりn−ヘキサン等で抽出した
胚芽油、植物油、動物油、魚油等が挙げられる。
これらの油脂は、油脂含有胚芽成分粉末の5〜30
%になるように添加するのが好ましく、これを超
えると粉末化が困難になり、また水に対する乳化
性が低下するので好ましくない。 Examples of the fats and oils added to the enzyme-treated product or the germ extract include germ oil extracted from whole fat germ with n-hexane, vegetable oil, animal oil, fish oil, and the like.
These oils and fats are 5 to 30% of the oil-containing germ component powder.
%, and if it exceeds this, it becomes difficult to powderize and the emulsifying property with water decreases, which is not preferable.
更にこのようにして油脂を添加した酵素処理物
又は胚芽エキスを乾燥して粉末化すれば栄養価の
高い乳化性の良い油脂含有胚芽成分粉末が得られ
る。 Further, by drying and powdering the enzyme-treated product or germ extract to which fats and oils have been added in this manner, a powder of germ component containing fats and oils with high nutritional value and good emulsifying properties can be obtained.
次に実施例を挙げて説明する。 Next, an example will be given and explained.
実施例 1
脱脂小麦胚芽(水分13%)(日清製粉社製)を
ピンミルにて粉砕して粉砕物100Kgに水400を加
えて撹拌混合した。これにα−アミラーゼ剤(液
化酵素T、力価10万U/g:阪急共栄物産社製)
500gを加え、撹拌しながら徐々に90℃まで昇温
(2℃/分)し、同温度に20分間保持した。次い
で処理物50℃まで冷却し、同温度でプロテアーゼ
剤(スミチームLP50、力価5万U/g:新日本
化学工業社製)500g及びグルコアミラーゼ剤
(グルクザイムAF6、力価6000U/g:天野製薬
社製)300gを加えて、同温度で5時間撹拌して
酵素処理を行つた。次いで、温度を90℃まで急速
に上げ、同温度に30分間保持して酵素の失活と殺
菌を行つた。得られた処理物を遠心分離して、抽
出液340を得た。Example 1 Defatted wheat germ (moisture 13%) (manufactured by Nisshin Seifun Co., Ltd.) was pulverized with a pin mill, and 400 kg of water was added to 100 kg of the pulverized product and mixed with stirring. Add to this an α-amylase agent (liquefied enzyme T, titer 100,000 U/g: manufactured by Hankyu Kyoei Bussan Co., Ltd.)
500 g was added, and the temperature was gradually raised to 90° C. (2° C./min) while stirring, and maintained at the same temperature for 20 minutes. Next, the treated material was cooled to 50°C, and at the same temperature, 500 g of protease agent (Sumizyme LP50, titer 50,000 U/g, manufactured by Shin Nihon Kagaku Kogyo Co., Ltd.) and glucoamylase agent (Gluczyme AF6, titer 6,000 U/g: Amano Pharmaceutical Co., Ltd.) 300g of the solution was added and stirred at the same temperature for 5 hours to perform enzyme treatment. Next, the temperature was rapidly raised to 90°C and maintained at the same temperature for 30 minutes to inactivate the enzyme and sterilize it. The obtained treated product was centrifuged to obtain an extract 340.
この抽出液に小麦胚芽油(全脂小麦胚芽よりn
−ヘキサンにて抽出し、精製したもの)25Kgを加
えて混合し、高圧ホモジナイザー(マントン・ゴ
ーリン社製)にて第1次圧力30Kg/cm2、第2次圧
力180Kg/cm2にて乳化させた後、スプレードライ
ヤーにて乾燥し、油脂含有胚芽エキス粉末を得
た。このものの組成は、水分2.5%、蛋白質26.3
%、糖質42.6%、灰分3.2%、脂質25.4%であり、
水によく分散した。 Add wheat germ oil (from full-fat wheat germ) to this extract.
- Extracted with hexane and purified), mixed, and emulsified using a high-pressure homogenizer (manufactured by Manton-Gaulin) at a primary pressure of 30 kg/cm 2 and a secondary pressure of 180 kg/cm 2 After that, it was dried with a spray dryer to obtain an oil-containing germ extract powder. The composition of this product is 2.5% water and 26.3% protein.
%, carbohydrates 42.6%, ash 3.2%, fat 25.4%,
Dispersed well in water.
実施例 2
実施例1と同様にして得た胚芽抽出液100に
イワシ油2Kgを混合し、高圧ホモジナイザー(実
施例1と同じ)にて第1次圧力20Kg/cm2、第2次
圧力220Kg/cm2で乳化させた後、スプレードライ
ヤーにて乾燥し、油脂含有胚芽エキス粉末(油脂
含量9.3%)を得た。Example 2 2 kg of sardine oil was mixed with 100 g of the embryo extract obtained in the same manner as in Example 1, and the mixture was heated to a primary pressure of 20 Kg/cm 2 and a secondary pressure of 220 Kg/cm 2 using a high-pressure homogenizer (same as in Example 1). After emulsifying in cm 2 , it was dried with a spray dryer to obtain an oil-containing germ extract powder (oil content 9.3%).
実施例 3
全脂小麦胚芽(水分13%)(日清製粉社製)を
ピンミルにて粉砕した粉砕物50Kgに水200を加
え、混合撹拌した。これにα−アミラーゼ剤(ス
ピターゼPK2、力価6万U/g:ナガセ生化学工
業社製)200gを加え、撹拌しながら徐々に85℃
まで昇温し、同温度に30分間保持した。次いで処
理物を55℃まで冷却し、プロテアーゼ剤(パンチ
ターゼNP、力価3万U/g:ヤクルト薬品工業
社製)100g及びグルコアミラーゼ剤(グルクザ
イムAF6、力価6000U/g:天野製薬社製)150
gを加え、同温度で撹拌しながら2時間酵素反応
を行つた。この処理物を実施例1と同様にして、
加熱処理、固液分離し、抽出液160をスプレー
ドライヤーにて噴霧乾燥して粉末胚芽エキス(水
分3.0%、油脂0.1%)を得た。また分取した固形
分を熱風乾燥した後ピンミルにて粉砕して粉末状
物(油脂含量30.5%)を得た。次いで、小麦胚芽
油5Kgに前記の粉末胚芽エキス30Kgおよび粉末状
物10Kgを添加し、更に水120Kgを添加して高圧ホ
モジナイザーにて圧力200Kg/cm2の条件で乳化さ
せて乳化物を得た。この乳化物をスプレードライ
ヤーにて乾燥して油脂含有胚芽成分粉末(油脂含
量18%)を得た。Example 3 200 kg of water was added to 50 kg of a pulverized product obtained by pulverizing full-fat wheat germ (moisture 13%) (manufactured by Nisshin Seifun Co., Ltd.) using a pin mill, and the mixture was mixed and stirred. Add 200 g of α-amylase agent (Spitase PK2, titer 60,000 U/g, manufactured by Nagase Seikagaku Kogyo Co., Ltd.) to this, and gradually raise the temperature to 85°C while stirring.
The temperature was raised to 100% and maintained at the same temperature for 30 minutes. The treated product was then cooled to 55°C, and 100 g of a protease agent (Puntase NP, titer 30,000 U/g, manufactured by Yakult Pharmaceutical Co., Ltd.) and a glucoamylase agent (Gluczyme AF6, titer 6000 U/g, manufactured by Amano Pharmaceutical Co., Ltd.) were added. 150
g was added thereto, and the enzymatic reaction was carried out for 2 hours while stirring at the same temperature. This treated product was treated in the same manner as in Example 1,
After heat treatment and solid-liquid separation, extract 160 was spray-dried using a spray dryer to obtain a powdered germ extract (3.0% moisture, 0.1% fat and oil). Further, the separated solid content was dried with hot air and then ground in a pin mill to obtain a powder (oil content: 30.5%). Next, 30 kg of the powdered germ extract and 10 kg of the powdered material were added to 5 kg of wheat germ oil, and 120 kg of water was further added and emulsified using a high-pressure homogenizer at a pressure of 200 kg/cm 2 to obtain an emulsion. This emulsion was dried with a spray dryer to obtain an oil-containing germ component powder (oil content: 18%).
実施例 4
フレーク状脱脂コーン胚芽(水分12%)50Kgに
水200を加え、撹拌混合した。これにα−アミ
ラーゼ剤(ユニアーゼBM8、力価8万U/g:
ヤクルト薬品工業社製)100gを加え、撹拌しな
がら徐々に90℃まで昇温(2℃/分)し、同温度
に20分間保持した。次いで処理物を55℃まで冷却
し、プロテアーゼ剤((デナチームAP、力価5万
U/g:ナガセ生化学工業社製)200gを加え、
同温度で3時間撹拌して酵素処理を行つた。この
処理物を実施例1と同様にして加熱処理、固液分
離を行い、抽出液を得た。この抽出液200にひ
まわり油2Kg及び小麦胚芽油5Kgを加え、高圧ホ
モジナイザーにて第1次圧力18Kg/cm2、第2次圧
力200Kg/cm2で乳化し、この乳化物をスプレード
ライヤーで乾燥して油脂含有胚芽エキス粉末(油
脂含量17.3%)を得た。Example 4 200 kg of water was added to 50 kg of flaky defatted corn germ (moisture 12%) and mixed by stirring. This was combined with an α-amylase agent (Uniase BM8, titer 80,000 U/g:
100 g of Yakult Pharmaceutical Co., Ltd.) was added thereto, and the temperature was gradually raised to 90°C (2°C/min) while stirring, and maintained at the same temperature for 20 minutes. Next, the treated product was cooled to 55°C, and 200 g of protease agent (Denazyme AP, titer 50,000 U/g, manufactured by Nagase Seikagaku Kogyo Co., Ltd.) was added.
Enzyme treatment was performed by stirring at the same temperature for 3 hours. This treated product was subjected to heat treatment and solid-liquid separation in the same manner as in Example 1 to obtain an extract. Add 2 kg of sunflower oil and 5 kg of wheat germ oil to this extract 200, emulsify with a high-pressure homogenizer at a primary pressure of 18 kg/cm 2 and a secondary pressure of 200 kg/cm 2 , and dry this emulsion with a spray dryer. An oil-containing germ extract powder (oil content 17.3%) was obtained.
実施例 5
実施例4の方法により酵素処理を行い、固液分
離を行わずに得られたコーン胚芽酵素処理物200
にサフラワー油2Kgおよび小麦胚芽油4Kgを添
加して高圧ホモジナイザー(圧力200Kg/cm2)に
て乳化させた。得られた乳化液をスプレードライ
ヤーにて乾燥して油脂含有胚芽粉末(油脂含量
11.5%)を得た。Example 5 Corn germ enzyme-treated product 200 obtained by enzymatic treatment according to the method of Example 4 without performing solid-liquid separation
2 kg of safflower oil and 4 kg of wheat germ oil were added to the mixture and emulsified using a high-pressure homogenizer (pressure: 200 kg/cm 2 ). The obtained emulsion was dried with a spray dryer to obtain oil-containing germ powder (oil content
11.5%).
実施例 6
(i) 全脂小麦胚芽(水分13%)(日清製粉社製)
100Kgをエクスパンデイングエクストルーダー
(ウエンガー社製X−25CF)に供給し、品温
120℃、圧力20Kg/cm2にて40秒間加圧加熱処理
し、常圧に放出して膨化処理を行つた。Example 6 (i) Full-fat wheat germ (moisture 13%) (manufactured by Nisshin Seifun Co., Ltd.)
Supply 100 kg to an expanding extruder (X-25CF manufactured by Wenger) and check the product temperature.
The mixture was subjected to pressure heat treatment at 120° C. and a pressure of 20 kg/cm 2 for 40 seconds, and then discharged to normal pressure for swelling treatment.
(ii) この膨化処理物に水400及びα−アミラー
ゼ剤(液化酵素T、力価10万U/g:阪急共栄
物産社製)300gを加え、撹拌しながら徐々に
90℃まで昇温(2℃/分)させ、同温度に20分
間保持した。この酵素処理液に小麦胚芽油40Kg
を加えて混合し、高圧ホモジナイザーにて圧力
250Kg/cm2で乳化した後、スプレードライヤー
で乾燥して油脂含有胚芽粉末(油脂含量27.3
%)を得た。(ii) Add 400 g of water and 300 g of α-amylase agent (Liquefied Enzyme T, titer 100,000 U/g, manufactured by Hankyu Kyoei Bussan Co., Ltd.) to this puffed product, and gradually add it while stirring.
The temperature was raised to 90°C (2°C/min) and maintained at the same temperature for 20 minutes. 40kg of wheat germ oil is added to this enzyme treatment solution.
Add, mix, and pressurize with a high-pressure homogenizer.
After emulsifying at 250Kg/ cm2 , it is dried with a spray dryer to obtain oil-containing germ powder (oil content 27.3
%) was obtained.
Claims (1)
は殿粉加水分解酵素と蛋白分解酵素を作用せし
め、次いでこれを加熱処理して得られる酵素処理
物、または該酵素処理物を固液分離して得られる
胚芽エキスに油脂を加えて乾燥することを特徴と
する油脂含有胚芽成分粉末の製造法。 2 穀類胚芽が膨化処理されたものである特許請
求の範囲第1項記載の油脂含有胚芽成分粉末の製
造法。 3 膨化処理が、圧力10〜100Kg/cm2、品温60〜
150℃、処理時間10〜120秒で加圧加熱処理し、低
圧下に放出させる方法である特許請求の範囲第2
項記載の油脂含有胚芽成分粉末の製造法。 4 油脂が胚芽油である特許請求の範囲第1項記
載の油脂含有胚芽成分粉末の製造法。[Scope of Claims] 1. An enzyme-treated product obtained by allowing a starch hydrolase or a starch hydrolase and a protease to act on cereal germ in the presence of water, and then heat-treating the same, or the enzyme A method for producing an oil-containing germ component powder, which comprises adding oil and fat to an embryo extract obtained by solid-liquid separation of a processed product and drying the mixture. 2. The method for producing an oil-containing germ component powder according to claim 1, wherein the grain germ is subjected to a swelling treatment. 3 The swelling process is performed at a pressure of 10-100Kg/cm 2 and a temperature of 60-
Claim 2, which is a method of performing pressure heat treatment at 150°C for a treatment time of 10 to 120 seconds and releasing it under low pressure.
A method for producing the oil-containing germ component powder described in . 4. The method for producing an oil-containing germ component powder according to claim 1, wherein the oil is an germ oil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59025597A JPS60168356A (en) | 1984-02-14 | 1984-02-14 | Production of embryo bud component powder containing fat or oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59025597A JPS60168356A (en) | 1984-02-14 | 1984-02-14 | Production of embryo bud component powder containing fat or oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60168356A JPS60168356A (en) | 1985-08-31 |
| JPH0358704B2 true JPH0358704B2 (en) | 1991-09-06 |
Family
ID=12170312
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59025597A Granted JPS60168356A (en) | 1984-02-14 | 1984-02-14 | Production of embryo bud component powder containing fat or oil |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60168356A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0734715B2 (en) * | 1986-02-24 | 1995-04-19 | 日清製粉株式会社 | Flavor oil manufacturing method |
-
1984
- 1984-02-14 JP JP59025597A patent/JPS60168356A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60168356A (en) | 1985-08-31 |
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