JPS629294B2 - - Google Patents
Info
- Publication number
- JPS629294B2 JPS629294B2 JP55006345A JP634580A JPS629294B2 JP S629294 B2 JPS629294 B2 JP S629294B2 JP 55006345 A JP55006345 A JP 55006345A JP 634580 A JP634580 A JP 634580A JP S629294 B2 JPS629294 B2 JP S629294B2
- Authority
- JP
- Japan
- Prior art keywords
- starch
- water
- gelatinization
- raw material
- degree
- 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
- 229920002472 Starch Polymers 0.000 claims description 34
- 235000019698 starch Nutrition 0.000 claims description 34
- 239000008107 starch Substances 0.000 claims description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 239000004088 foaming agent Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 13
- 239000002994 raw material Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 11
- 239000006260 foam Substances 0.000 claims description 8
- 238000005187 foaming Methods 0.000 claims description 7
- 239000003381 stabilizer Substances 0.000 claims description 6
- 235000014113 dietary fatty acids Nutrition 0.000 description 12
- 239000000194 fatty acid Substances 0.000 description 12
- 229930195729 fatty acid Natural products 0.000 description 12
- -1 glycerin fatty acid esters Chemical class 0.000 description 11
- 229920000881 Modified starch Polymers 0.000 description 6
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 6
- 235000013305 food Nutrition 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerol Natural products OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 229930006000 Sucrose Natural products 0.000 description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 3
- 229910052782 aluminium Inorganic materials 0.000 description 3
- 235000013339 cereals Nutrition 0.000 description 3
- 235000011187 glycerol Nutrition 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000005720 sucrose Substances 0.000 description 3
- 229920002261 Corn starch Polymers 0.000 description 2
- 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 2
- 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 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000008120 corn starch Substances 0.000 description 2
- 229940099112 cornstarch Drugs 0.000 description 2
- 235000013312 flour Nutrition 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229960002920 sorbitol Drugs 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 1
- QCVGEOXPDFCNHA-UHFFFAOYSA-N 5,5-dimethyl-2,4-dioxo-1,3-oxazolidine-3-carboxamide Chemical compound CC1(C)OC(=O)N(C(N)=O)C1=O QCVGEOXPDFCNHA-UHFFFAOYSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical class OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- 239000004604 Blowing Agent Substances 0.000 description 1
- 241001454694 Clupeiformes Species 0.000 description 1
- PHOQVHQSTUBQQK-SQOUGZDYSA-N D-glucono-1,5-lactone Chemical compound OC[C@H]1OC(=O)[C@H](O)[C@@H](O)[C@@H]1O PHOQVHQSTUBQQK-SQOUGZDYSA-N 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- 108010068370 Glutens Proteins 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 240000003183 Manihot esculenta Species 0.000 description 1
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 235000019513 anchovy Nutrition 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000008429 bread Nutrition 0.000 description 1
- 235000012839 cake mixes Nutrition 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 235000014103 egg white Nutrition 0.000 description 1
- 210000000969 egg white Anatomy 0.000 description 1
- 235000013601 eggs Nutrition 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 235000010855 food raising 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
- 235000012209 glucono delta-lactone Nutrition 0.000 description 1
- 239000000182 glucono-delta-lactone Substances 0.000 description 1
- 229960003681 gluconolactone Drugs 0.000 description 1
- 235000021312 gluten Nutrition 0.000 description 1
- 150000004676 glycans 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
- 239000000665 guar gum Substances 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 235000014109 instant soup Nutrition 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 235000016337 monopotassium tartrate Nutrition 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- KYKNRZGSIGMXFH-ZVGUSBNCSA-M potassium bitartrate Chemical compound [K+].OC(=O)[C@H](O)[C@@H](O)C([O-])=O KYKNRZGSIGMXFH-ZVGUSBNCSA-M 0.000 description 1
- 229940086065 potassium hydrogentartrate Drugs 0.000 description 1
- 229920001592 potato starch Polymers 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229930182490 saponin Natural products 0.000 description 1
- 150000007949 saponins Chemical class 0.000 description 1
- 235000017709 saponins Nutrition 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 150000003892 tartrate salts Chemical class 0.000 description 1
Landscapes
- Grain Derivatives (AREA)
- Jellies, Jams, And Syrups (AREA)
Description
本発明は澱粉の新規なα化方法に係り、その目
的とするところは、目的に応じてα化度を均一に
制御し、粉崩壊のないα化澱粉を得ることができ
る澱粉のα化方法を提供するものである。
従来、澱粉のα化は、澱粉原料と水の混合物を
ドラムドライヤー、あるいはエクストルーダー等
を用いて加熱処理する方法によつて行われてき
た。
しかし、ドラムドライヤーを使用する方法は、
操作上多量の水を混合しなければならないため、
α化度を制御することが困難であり、また水の量
を極力減らしてもα化が不均一で、目的とするα
化度の製品を得ることができなかつた。また、エ
クストルーダーを用いる方法は、水分の少ない条
件でα化を行うことができるが、加圧押出しの過
程で澱粉粒が破壊され、限られた使用用途の製品
しか得ることができなかつた。
以上の如く、従来法によつて得られるα化澱粉
は、α化が不均一であると共に、α化された澱粉
粒のα化度はほぼ100%であり、しかも澱粉粒が
崩壊しているため、これを水に溶解して使用する
と吸水が早すぎてダマを形成し易く、利用上不都
合なことが多かつた。
一方、パンやアンをはじめとする食品中の澱粉
はその粒が崩壊していないことが食感に大きく影
響するものであり、特に近年需要が急激に増大し
たインスタント食品の場合には、α化度を30〜90
%に制御した水分散性の良好なα化澱粉を使用
し、調理の際加熱処理してα化度を100%とする
ことが望まれている。
斯る実状において、本発明者は、澱粉のα化に
ついて鋭意研究を行つた結果、澱粉原料と水との
混合物を泡立てた状態で加熱処理すると、限られ
た水分が均一に澱粉のα化に利用され、α化を均
一に行うことができると共に、含水量及び加熱量
を調節すれば、任意のα化度のものを製造でき、
かつ粒崩壊が起らずそのために水に対する分散性
がよくなることを見出し、本発明を完成した。
すなわち、本発明は、起泡剤を加えて澱粉原料
と水の混合物を泡立て、次いでこれを加熱処理す
ることを特徴とする澱粉のα化方法である。
本発明において、澱粉原料とは、とうもろこ
し、小麦、馬鈴薯、タピオカ等から分離した澱粉
並びにこれらの澱粉を含むものが挙げられる。
起泡剤は通常食品に使用されるものであれば何
れのものでもよく、例えばグリセリン脂肪酸エス
テル(乳酸化モノグリセリン、アセチル化モノグ
リセリン、ポリグリセリン脂肪酸エステル)、ソ
ルビタン脂肪酸エステル、ポリオキシソルビタン
脂肪酸エステル、シヨ糖脂肪酸エステル等の界面
活性剤;炭素数3〜8の脂肪酸あるいはアルコー
ル;炭酸塩、重炭酸塩、酒石酸塩、グルコノデル
タラクトン等の膨剤;卵白が挙げられ、これらは
単独又は2種以上を混合して使用される。この起
泡剤は、通常澱粉原料に対し0.02〜20重量%(以
下%は重量で示す)添加するのが好ましい。この
起泡剤が安定な気泡を形成する場合はそれ単独で
もよいが、気泡が不安定な場合、例えば上記膨剤
等の場合には更に起泡安定剤を併用するのが好ま
しい。起泡安定剤としては、一般に知られている
ゼラチン、サポニン、グルテン等の蛋白及びその
分解物;グアガム等の多糖類が挙げられ、これら
は1種又は2種以上の混合物として、澱粉原料に
対し0.1〜20%添加される。
本発明を実施するには、水に起泡剤、起泡安定
剤を加えて泡立てた後澱粉原料を混合するか、あ
るいは澱粉原料、起泡剤、起泡安定剤及び水を同
時に混合し、充分に混和する。この際加えられる
水の量は、目的とするα化度によつて異なるが、
α化度を30〜90%にするためには、澱粉原料に対
し40〜230%になるようにするのが好ましい。
起泡剤として、例えば前述の如き膨剤を使用し
たときは混合すれば発泡して泡立ちが起るが、前
記界面活性剤等の場合には、上記混合物をプロペ
ラミキサー、ホモミキサー、コロイドミル、TK
ホモゲナイザー、エアミキサー、加圧ノズル式乳
化機等を用いて充分に混和して泡立てを行う。
次いで、このようにして泡立てた澱粉原料は加
熱処理してα化を行う。加熱処理はドラムドライ
ヤーを用いる方法、平らな容器に入れて加熱機中
で加熱する方法等によつて行われる。加熱温度
は、当該混合物の厚さ、目的とするα化度によつ
て異なるが、一般には70〜250℃、特に100〜200
℃が好ましく、加熱時間は30秒から5時間が好ま
しい。α化度を抑制するためには生地の起泡する
条件の範囲内で含水量を低めにおさえるとともに
加熱量を少なくすることにより達成される。
斯くして得られたα化澱粉は乾燥、粉砕される
が、得られるα化澱粉はカサが大きいので、粉砕
時の粒崩壊は極めて少ない。粉砕は常法によつて
行われ、粒度は使用用途によつて異なる。
叙上の如くして得られるα化澱粉は任意のα化
度に均一にα化されており、かつ粒崩壊がないの
で、水に対する分散性がよく、種々の食品、特に
インスタントスープ、インスタントシユー、ケー
キミツクス等のインスタント食品の澱粉素材とし
て極めて優れている。
次に実施例及び応用例を挙げて説明する。
実施例 1
ケーキ用ミキサーに5容器およびホイツパー
を取り付け、これに水1000mlにケーキ用起泡剤
(シヨ糖脂肪酸エステル10%、ソルビタン脂肪酸
エステル10%、グリセリン脂肪酸エステル10%、
D−ソルビツト液40%、プロピレングリコール5
%)30gを溶解したものを入れた。これに馬鈴薯
澱粉1000gを加え、低速にて1分間、高速にて3
分間撹拌した。得られた気泡体を平らなアルミ製
容器に5.5mmの厚さになるように流し込んだ。こ
れを140℃の乾燥機に入れ1時間、次いで120℃で
2時間加熱した後得られた乾燥物を粉砕して試料
(A)とした。また上記成分からケーキ用起泡剤を除
いたもの〔対照(1)〕を試料(A)と同様に処理して対
照品とした。また市販αコーンスターチ(常法に
よつてドラムドライヤーにて製造したもの)を対
照(2)とした。これらの試料について、粉砕前の乾
燥物の状態、粉砕後のα化でんぷんのα化度およ
びこれらのα化でんぷんを水へ分散せしめた時の
ダマの形成の有無を観察し結果を第1表に示す。
The present invention relates to a novel method for gelatinizing starch, and its purpose is to uniformly control the degree of gelatinization according to the purpose, and to obtain gelatinized starch without powder disintegration. It provides: Conventionally, starch gelatinization has been carried out by heating a mixture of starch raw material and water using a drum dryer, an extruder, or the like. However, the method of using a drum dryer is
Because the operation requires mixing a large amount of water,
It is difficult to control the degree of gelatinization, and even if the amount of water is reduced as much as possible, gelatinization is uneven, and
It was not possible to obtain a product with a high degree of chemicalness. In addition, in the method using an extruder, gelatinization can be carried out under conditions with low moisture content, but starch granules are destroyed during the pressure extrusion process, making it possible to obtain products with only limited uses. As mentioned above, in the pregelatinized starch obtained by the conventional method, the gelatinization is uneven, and the degree of gelatinization of the pregelatinized starch granules is almost 100%, and moreover, the starch granules are disintegrated. Therefore, when it is dissolved in water and used, it absorbs water too quickly and tends to form lumps, which is often inconvenient for use. On the other hand, the texture of starch in foods such as bread and anchovies is greatly affected by the fact that the grains are not disintegrated.Especially in the case of instant foods, the demand for which has increased rapidly in recent years, gelatinization degree 30~90
It is desirable to use pregelatinized starch with good water dispersibility controlled at 100% and heat-treat it during cooking to achieve a pregelatinization degree of 100%. Under such circumstances, the present inventor conducted intensive research on the gelatinization of starch and found that when a mixture of starch raw material and water is heated in a foamed state, the limited moisture uniformly gelatinizes the starch. It can be used to uniformly pregelatinize, and by adjusting the water content and heating amount, it is possible to produce products with any degree of pregelatinization.
Furthermore, the present invention was completed based on the discovery that grain disintegration does not occur and therefore the dispersibility in water is improved. That is, the present invention is a method for gelatinizing starch, which is characterized by adding a foaming agent to foam a mixture of starch raw material and water, and then heat-treating the mixture. In the present invention, the starch raw material includes starch separated from corn, wheat, potato, tapioca, etc., and materials containing these starches. The foaming agent may be any one commonly used in foods, such as glycerin fatty acid esters (lactated monoglycerin, acetylated monoglycerin, polyglycerin fatty acid esters), sorbitan fatty acid esters, polyoxysorbitan fatty acid esters. , surfactants such as sucrose fatty acid esters; fatty acids or alcohols having 3 to 8 carbon atoms; leavening agents such as carbonates, bicarbonates, tartrates, and gluconodelta-lactone; It is used by mixing more than one species. This foaming agent is preferably added in an amount of 0.02 to 20% by weight (hereinafter % is expressed by weight) based on the starch raw material. If this foaming agent forms stable bubbles, it may be used alone, but if the foam is unstable, for example, in the case of the above-mentioned swelling agent, it is preferable to use a foaming stabilizer in combination. Examples of foaming stabilizers include generally known proteins such as gelatin, saponin, and gluten, and their decomposition products; and polysaccharides such as guar gum. Added from 0.1 to 20%. To carry out the present invention, a foaming agent and a foaming stabilizer are added to water and foamed, and then a starch raw material is mixed, or a starch raw material, a foaming agent, a foaming stabilizer, and water are mixed simultaneously, Mix thoroughly. The amount of water added at this time varies depending on the desired degree of gelatinization, but
In order to make the degree of gelatinization 30 to 90%, it is preferably 40 to 230% of the starch raw material. For example, when the above-mentioned blowing agent is used as a foaming agent, it foams and foams when mixed, but when the surfactant is used, the mixture is mixed with a propeller mixer, homomixer, colloid mill, etc. T.K.
Thoroughly mix and foam using a homogenizer, air mixer, pressure nozzle emulsifier, etc. Next, the starch raw material foamed in this way is heat-treated to undergo gelatinization. The heat treatment is carried out by a method using a drum dryer, a method of placing the material in a flat container and heating it in a heating machine, or the like. The heating temperature varies depending on the thickness of the mixture and the desired degree of gelatinization, but is generally 70 to 250°C, particularly 100 to 200°C.
The temperature is preferably 0.degree. C., and the heating time is preferably 30 seconds to 5 hours. In order to suppress the degree of gelatinization, it is achieved by keeping the water content low within the range of foaming conditions of the dough and reducing the amount of heating. The gelatinized starch thus obtained is dried and pulverized, but since the gelatinized starch obtained has a large bulk, there is very little granulation during pulverization. Grinding is carried out by a conventional method, and the particle size varies depending on the intended use. The pregelatinized starch obtained as described above is uniformly pregelatinized to any pregelatinization degree and does not disintegrate, so it has good dispersibility in water and can be used in various foods, especially instant soups and instant cereals. It is extremely excellent as a starch material for instant foods such as yew and cake mixes. Next, examples and application examples will be given and explained. Example 1 Attach 5 containers and a whipper to a cake mixer, add 1000 ml of water and a cake foaming agent (10% sucrose fatty acid ester, 10% sorbitan fatty acid ester, 10% glycerin fatty acid ester,
D-sorbitol solution 40%, propylene glycol 5
%) dissolved in 30g was added. Add 1000g of potato starch to this and turn on low speed for 1 minute, then on high speed for 3 minutes.
Stir for a minute. The resulting foam was poured into a flat aluminum container to a thickness of 5.5 mm. This was placed in a dryer at 140°C for 1 hour, then heated at 120°C for 2 hours, and the resulting dried product was crushed and sampled.
(A). In addition, a control product obtained by removing the cake foaming agent from the above components [Control (1)] was treated in the same manner as Sample (A). In addition, commercially available alpha corn starch (produced using a drum dryer in a conventional manner) was used as a control (2). For these samples, we observed the state of the dry matter before crushing, the degree of gelatinization of the pregelatinized starch after crushing, and the presence or absence of lump formation when these pregelatinized starches were dispersed in water, and the results are shown in Table 1. Shown below.
【表】
実施例 2
ケーキ用ミキサーに5容器及びホイツパーを
取付け、これに水2000mlにケーキ用起泡剤(シヨ
糖脂肪酸エステル10%、ソルビタン脂肪酸エステ
ル10%、グリセリン脂肪酸エステル10%、D−ソ
ルビツト液40%、プロピレングリコール5%)30
gを溶解したものを入れた。これに薄力小麦粉
1000gを加え、低速で1分間、高速で3分間泡立
てを行つた。得られた気泡体を平らなアルミ製容
器に5.5mmの厚さに流し込み、100℃の乾燥機で3
時間加熱乾燥し、粉砕して試料(B)とした。また、
気泡体の厚さを2.8mmとしたか、加熱温度を120℃
にした以外は同様に処理し、それぞれを試料(C)、
試料(D)とした。
これら試料の性状は第2表のとおりである。[Table] Example 2 Attach 5 containers and a whipper to a cake mixer, add 2000 ml of water and a foaming agent for cakes (10% sucrose fatty acid ester, 10% sorbitan fatty acid ester, 10% glycerin fatty acid ester, D-sorbitol). liquid 40%, propylene glycol 5%) 30
A solution of g was added. Light flour for this
1000g was added and whisked at low speed for 1 minute and at high speed for 3 minutes. The resulting foam was poured into a flat aluminum container to a thickness of 5.5 mm, and dried in a dryer at 100℃ for 3
It was dried by heating for a period of time and pulverized to obtain a sample (B). Also,
The thickness of the bubble was 2.8mm, and the heating temperature was 120℃.
Samples (C) and
This was designated as sample (D). The properties of these samples are shown in Table 2.
【表】
実施例 3
コーンスターチ1000g、卵白500g(乾物とし
て65g)、ベーキングパウダー30g(重炭酸ソー
ダ8.1g、酒石酸水素カリウム1.2g)及び水565
mlを均一に混合し、平らなアルミ製容器に厚さ
5.5mmになるように流し込んだ。容器ごと200℃に
加熱したオーブンに入れ、10分間加熱した後、
100℃の乾燥機に移し水分約5%まで乾燥した。
乾燥物をライカイ機で100メツシユ以下の粒度に
粉砕した。得られた澱粉のα化度は70%であつ
た。
応用例 1
実施例2で得た試料(B)100部に食用油脂63部、
砂糖2.5部、食塩0.1部、レシチン0.2部及び乾燥卵
18.8部を加えて混合してインスタントシユーを製
造した。
このインスタントシユーに適量の水を加えて混
和し、200℃で焼成したところ良好なシユーが得
られた。
一方、ドラムドライヤーにて常法によつてα化
した小麦粉を使用して上記と同様にしてインスタ
ントシユーを作り、同様にして加水し、焼成した
ところ、油が表面に出て膨らまなかつた。[Table] Example 3 1000 g of cornstarch, 500 g of egg white (65 g as dry matter), 30 g of baking powder (8.1 g of bicarbonate of soda, 1.2 g of potassium hydrogen tartrate), and 565 g of water.
Mix the ml evenly and place it in a flat aluminum container to a thickness of
It was poured to a thickness of 5.5mm. Place the entire container in an oven heated to 200℃ and heat for 10 minutes.
It was transferred to a dryer at 100°C and dried to a moisture content of approximately 5%.
The dried material was ground to a particle size of less than 100 mesh using a Raikai machine. The degree of gelatinization of the obtained starch was 70%. Application example 1 63 parts of edible oil and fat were added to 100 parts of the sample (B) obtained in Example 2.
2.5 parts sugar, 0.1 part salt, 0.2 part lecithin, and dried eggs
18.8 parts were added and mixed to produce an instant chew. A suitable amount of water was added to this instant sew, mixed, and baked at 200°C, resulting in a good sew. On the other hand, when an instant shoe was made in the same manner as above using wheat flour that had been pregelatinized using a drum dryer in a conventional manner, and water was added and baked in the same manner, oil came out to the surface and the powder did not rise.
Claims (1)
て、次いでこれを加熱処理することを特徴とする
澱粉のα化方法。 2 起泡剤と起泡安定剤を併用することを特徴と
する特許請求の範囲第1項記載の澱粉のα化方
法。 3 水の量が澱粉原料の40〜230重量%である特
許請求の範囲第1項又は第2項記載の澱粉のα化
方法。 4 起泡剤の量が澱粉原料の0.02〜20重量%であ
る特許請求の範囲第1項又は第2項記載の澱粉の
α化方法。 5 起泡安定剤の量が澱粉原料の0.1〜20重量%
である特許請求の範囲第2項記載の澱粉のα化方
法。 6 加熱処理を70〜250℃の温度で行う特許請求
の範囲第1項ないし第5項の何れかの項記載の澱
粉のα化方法。[Claims] 1. A method for gelatinizing starch, which comprises adding a foaming agent to foam a mixture of starch raw material and water, and then heat-treating the mixture. 2. The method for pregelatinizing starch according to claim 1, characterized in that a foaming agent and a foaming stabilizer are used in combination. 3. The method for pregelatinizing starch according to claim 1 or 2, wherein the amount of water is 40 to 230% by weight of the starch raw material. 4. The method for pregelatinizing starch according to claim 1 or 2, wherein the amount of the foaming agent is 0.02 to 20% by weight of the starch raw material. 5 The amount of foaming stabilizer is 0.1 to 20% by weight of the starch raw material.
The method for gelatinizing starch according to claim 2. 6. The method for pregelatinizing starch according to any one of claims 1 to 5, wherein the heat treatment is performed at a temperature of 70 to 250°C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP634580A JPS56106570A (en) | 1980-01-24 | 1980-01-24 | Conversion of starch to alpha-form |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP634580A JPS56106570A (en) | 1980-01-24 | 1980-01-24 | Conversion of starch to alpha-form |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56106570A JPS56106570A (en) | 1981-08-24 |
| JPS629294B2 true JPS629294B2 (en) | 1987-02-27 |
Family
ID=11635776
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP634580A Granted JPS56106570A (en) | 1980-01-24 | 1980-01-24 | Conversion of starch to alpha-form |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56106570A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ZA826015B (en) * | 1981-10-01 | 1983-10-26 | Cpc International Inc | Hot water dispersible starch-surfactant products, including acid stable and acid and freeze thaw stable food thickeners |
| DE3206751C2 (en) * | 1982-02-25 | 1986-08-21 | SÜDSTÄRKE GmbH, 8898 Schrobenhausen | Process for the production of foamed, gelatinized starch products |
| JP5265821B1 (en) * | 2013-01-28 | 2013-08-14 | 日本食品化工株式会社 | Oil processed starch and method for producing the same |
-
1980
- 1980-01-24 JP JP634580A patent/JPS56106570A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56106570A (en) | 1981-08-24 |
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