JPS6343902A - Production of modified starch - Google Patents
Production of modified starchInfo
- Publication number
- JPS6343902A JPS6343902A JP18809986A JP18809986A JPS6343902A JP S6343902 A JPS6343902 A JP S6343902A JP 18809986 A JP18809986 A JP 18809986A JP 18809986 A JP18809986 A JP 18809986A JP S6343902 A JPS6343902 A JP S6343902A
- Authority
- JP
- Japan
- Prior art keywords
- starch
- cold water
- mixture
- water
- heating
- 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.)
- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 22
- 229920000881 Modified starch Polymers 0.000 title abstract description 22
- 235000019426 modified starch Nutrition 0.000 title abstract description 13
- 239000004368 Modified starch Substances 0.000 title abstract description 9
- 229920002472 Starch Polymers 0.000 claims abstract description 130
- 235000019698 starch Nutrition 0.000 claims abstract description 114
- 239000008107 starch Substances 0.000 claims abstract description 105
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 77
- 238000010438 heat treatment Methods 0.000 claims abstract description 22
- 239000000203 mixture Substances 0.000 claims abstract description 20
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000004327 boric acid Substances 0.000 claims abstract description 14
- 229910021538 borax Inorganic materials 0.000 claims abstract description 11
- 239000004328 sodium tetraborate Substances 0.000 claims abstract description 11
- 235000010339 sodium tetraborate Nutrition 0.000 claims abstract description 11
- 239000002245 particle Substances 0.000 claims abstract description 9
- 239000002253 acid Substances 0.000 claims abstract description 8
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims abstract description 7
- 150000007513 acids Chemical class 0.000 claims abstract description 7
- 238000012546 transfer Methods 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 24
- 238000003756 stirring Methods 0.000 claims description 16
- 239000000654 additive Substances 0.000 claims description 8
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical class OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- 239000008187 granular material Substances 0.000 claims description 5
- 238000010298 pulverizing process Methods 0.000 claims description 5
- 150000004649 carbonic acid derivatives Chemical class 0.000 claims description 3
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 claims description 2
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical group [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims 1
- 150000001642 boronic acid derivatives Chemical class 0.000 claims 1
- UIIMBOGNXHQVGW-UHFFFAOYSA-N sodium;hydron;carbonate Chemical group [Na+].OC(O)=O UIIMBOGNXHQVGW-UHFFFAOYSA-N 0.000 claims 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 abstract description 6
- 238000000227 grinding Methods 0.000 abstract description 2
- 150000003839 salts Chemical class 0.000 abstract 2
- 238000013019 agitation Methods 0.000 abstract 1
- 229910000029 sodium carbonate Inorganic materials 0.000 abstract 1
- 239000003292 glue Substances 0.000 description 21
- 229920002261 Corn starch Polymers 0.000 description 20
- 239000008120 corn starch Substances 0.000 description 20
- 229940099112 cornstarch Drugs 0.000 description 20
- 239000000835 fiber Substances 0.000 description 14
- 238000001035 drying Methods 0.000 description 11
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 8
- 238000004026 adhesive bonding Methods 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000007796 conventional method Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- 229940100445 wheat starch Drugs 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 4
- 235000017557 sodium bicarbonate Nutrition 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 206010042674 Swelling Diseases 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
- 238000004090 dissolution Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229920001592 potato starch Polymers 0.000 description 3
- 229940100486 rice starch Drugs 0.000 description 3
- 238000010971 suitability test Methods 0.000 description 3
- 230000008961 swelling Effects 0.000 description 3
- 239000002562 thickening agent Substances 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 235000013373 food additive Nutrition 0.000 description 2
- 239000002778 food additive Substances 0.000 description 2
- 235000003642 hunger Nutrition 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 238000010409 ironing Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229940057995 liquid paraffin Drugs 0.000 description 2
- 239000002932 luster Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 230000037351 starvation Effects 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229920001353 Dextrin Polymers 0.000 description 1
- 239000004375 Dextrin Substances 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 240000004668 Valerianella locusta Species 0.000 description 1
- 235000003560 Valerianella locusta Nutrition 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 235000019425 dextrin Nutrition 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 235000013808 oxidized starch Nutrition 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000009955 starching Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000002522 swelling effect Effects 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Description
【発明の詳細な説明】 l−1泗り寿1直輩1 (技術分野) 本発明は、冷水易溶性加工澱粉の製造方法に関する。[Detailed description of the invention] l-1 Riju 1 Direct senior 1 (Technical field) The present invention relates to a method for producing processed starch that is readily soluble in cold water.
(従来の技術)
従来からα化澱粉は各種の用途Gこ用いられてきたが、
これを洗濯糊に用いるときは、冷水に易溶でなく、加熱
溶解が必要である。また冷水中での分散が悪いなどの欠
点があって利用されていなかった。(Prior art) Pregelatinized starch has been used for various purposes, but
When using this as a laundry starch, it is not easily soluble in cold water and requires heating and dissolution. Furthermore, it has not been used because of its drawbacks such as poor dispersion in cold water.
洗濯業界における洗濯糊用澱粉に関する技術的議論は、
皆無に近い。その理由は、洗濯に使用される澱粉の種類
もさることながら洗濯の仕上げの技術・熟練度が洗濯糊
用澱粉の品質等を大きく上まわって洗濯の仕上がりの良
否に大きく影響を及ぼすと信じられていたからである。Technical discussions regarding starch for laundry glue in the laundry industry include:
Almost none. The reason for this is that, in addition to the type of starch used for washing, it is believed that the finishing technique and skill level of the washing far exceeds the quality of the starch used for laundry glue, and has a great influence on the quality of the finished washing. This is because it was
永年の間、工業用、家庭用の洗濯糊の原料として米澱粉
が使用されてきた。米澱粉は価格が高いが、布への滲透
力や仕上がりの柔軟性や光沢の良さのために評判は良か
った。この大きな理由は米澱粉は粒子が極小であるため
である。最近、工程の簡略化および仕上がりの良さ、さ
らには排水の問題をも含めて、洗濯糊用澱粉の研究が進
められている0例えば、コーンスターチの糊を用いれば
。For many years, rice starch has been used as a raw material for industrial and household laundry starch. Although rice starch is expensive, it has a good reputation for its ability to penetrate into fabrics, its flexibility and glossy finish. The main reason for this is that rice starch has extremely small particles. Recently, research into starch for laundry glue has been underway to simplify the process, improve the finish, and even address drainage problems.For example, if cornstarch glue is used.
固い風合いの仕上がりになり、小麦澱粉の糊を用いれば
柔らかい風合いの糊ができる。それらを混合して用いれ
ば9両者の長所を兼ね備えた風合いの仕上がりになる。The finished product has a hard texture, while wheat starch paste can be used to create a soft texture. If you use a mixture of them, you will get a texture that combines the advantages of both.
しかしながら、これらはすべて、加熱により澱粉粒を糊
化させてから、用いる必要があった。この加熱などの糊
液調製条件によって、糊の質が著しく変動し、糊調製操
作に熟練を必要とした。このために、糊化温度を低くし
た化工澱粉や、可溶性澱粉、デキストリンなども洗濯糊
として用いることもあった。However, all of these require the starch granules to be gelatinized by heating before use. The quality of the glue varies considerably depending on the conditions for preparing the glue, such as heating, and the glue preparation requires skill. For this reason, modified starches with low gelatinization temperatures, soluble starches, dextrins, and the like are sometimes used as laundry glues.
洗濯糊付けの目的は澱粉の分子が細い繊維の間に適度に
滲透し、かつ繊維の上に糊の薄い被膜を形成することで
あって、これにより1次の効果をあたえる=(1)繊維
に適当な固さと、風合いと弾力性をつける。The purpose of laundry starching is to allow starch molecules to penetrate between the thin fibers and form a thin film of starch on the fibers, which provides the first effect = (1) to the fibers. Add appropriate hardness, texture and elasticity.
(2)繊維につやと滑りをつけ1着心地をよくする。(2) Add luster and slip to the fibers to improve comfort.
(3)衣類のアイロン整形をよくシ、保形を助ける。(3) Iron clothes well to help retain their shape.
(4)着用中に、汚れが直接繊維の内部に滲透すること
を防止し1次に洗浄するとき、繊維に付けた糊が洗い落
とされることにより汚れもよく落ちる。(4) Dirt is prevented from penetrating directly into the fibers during wear, and when the garment is first washed, the glue attached to the fibers is washed away and dirt is easily removed.
以上の目的に沿う糊付としては、前記した澱粉糊、フノ
リ、などの天然物およびカルボキシメチルセルロース、
ポリビニルアルコールなどの合成品がある。そのうち1
価格の低度なこと1次回の洗濯時の糊落ちの良好なこと
などから、澱粉糊が比較的多く用いられる。Gluing that meets the above purpose includes natural products such as the starch glue and french described above, and carboxymethyl cellulose,
There are synthetic products such as polyvinyl alcohol. 1 of them
Starch glue is relatively often used because it is inexpensive and the glue comes off easily after the first wash.
洗濯糊用澱粉として通常用いられている澱粉はコーンス
ターチと、小麦澱粉である。しかし小麦澱粉は、原料事
情と製造中の廃水処理の困難なことから、生産量は極度
に減少し、現在は洗濯糊用澱粉としては、もっばら、コ
ーンスターチのみが用いられている。Starches commonly used as laundry starch are corn starch and wheat starch. However, the production of wheat starch has drastically decreased due to raw material issues and the difficulty of treating wastewater during production, and currently only corn starch is used as starch for laundry glue.
コーンスターチを洗濯糊として用いる方法の一例は次の
通りである:洗濯業界では「糊たき3年」と言われてお
り、糊たきは非常に困難なものとされている。An example of a method of using corn starch as a laundry starch is as follows: In the laundry industry, it is said to be ``3 years of starvation'', and starvation is considered to be extremely difficult.
(1)モト糊を炊く (5%モト糊)
一定濃度のモト糊をあらかじめ炊いておき、これを糊付
けする衣類に応じて適当に薄めて糊液をつくる。その炊
き方の一例は、101の目盛付バケツに水を7分目に入
れ、コーンスターチ500 gを入れて良く攪拌して、
蒸気を入れ、80〜85℃になったら、蒸気を止め、水
または湯を加えて全量を101にする。(1) Cook Moto-nori (5% Moto-nori) Cook a certain concentration of Moto-nori in advance, and dilute it appropriately depending on the garment to be glued to make a starch solution. An example of how to cook it is to put water into a 101 graduated bucket at the 7th minute mark, add 500 g of cornstarch, and stir well.
Turn on the steam, and when the temperature reaches 80-85°C, turn off the steam and add water or hot water to bring the total volume to 101.
(2)糊付は作業
ワイシャツ50枚(10キロワツシヤー)の場合もと糊
51に温湯51を添加してワッシャーに入れ糊づけを行
う。(2) Gluing is carried out in the case of 50 shirts (10 kilograms). Hot water 51 is added to starch 51 and the mixture is placed in a washer for gluing.
以上のように澱粉は、必ず加熱して糊にしなければ洗濯
糊として使用できない。As mentioned above, starch cannot be used as laundry glue unless it is heated to form a glue.
これに対して冷水可溶性のα化澱粉は加熱糊化の工程が
省略でき、その使用方法は簡便である。On the other hand, gelatinized starch that is soluble in cold water can omit the heat gelatinization process and is easy to use.
冷水可溶の澱粉の作成方法は、各種開発されている。一
つの方法は、水分を含有した澱粉を、熱ロール間を通過
せしめて、澱粉を糊化させると共に。Various methods have been developed to produce cold water soluble starch. One method is to pass starch containing water between heated rolls to gelatinize the starch.
乾燥させたのち、粉砕して、乾燥α化澱粉を得る方法で
ある。別の方法は、澱粉を加熱固化と同時に酸や酵素で
部分的に加水分解してから、加熱ロール間を通過させて
乾燥し、粉砕して乾燥α化澱粉を得る方法である。さら
に別の方法は澱粉を酸化剤で酸化を行い、その後、糊化
し加熱ロール間を通過せしめ、乾燥し粉砕する方法であ
る。さらに別の方法は、澱粉に硼砂を7〜15%添加し
て。After drying, the starch is crushed to obtain dried pregelatinized starch. Another method is to partially hydrolyze starch with an acid or an enzyme at the same time as heating and solidifying it, and then drying it by passing it between heated rolls and pulverizing it to obtain dry pregelatinized starch. Yet another method is to oxidize starch with an oxidizing agent, then gelatinize it, pass it between heated rolls, dry it, and crush it. Yet another method is to add 7-15% borax to starch.
熱ロール間を通過させ乾燥・粉砕し乾燥α化澱粉を得る
方法(米国特許隠2819.980号公報)である。This is a method (US Patent No. 2,819.980) to obtain dry pregelatinized starch by passing it between hot rolls, drying and pulverizing it.
これらの方法で製造した冷水可溶性澱粉を洗濯糊用とし
て使用した場合には、いずれも次の問題を生じる:
(1)製造コストが高い。When cold water soluble starches produced by these methods are used as laundry starches, the following problems arise: (1) Production costs are high.
(2)水に速やかに分散しない。(2) Does not disperse quickly in water.
(3)まま粉が生じ易い。(3) Leaves are likely to form.
(4)水には完全可溶ではなくて糊液貯蔵時、容器下部
にかなりの量の沈着物が残る。(4) It is not completely soluble in water, and a considerable amount of deposits remain at the bottom of the container when the size solution is stored.
洗濯業界は比較的、経営規模の小さな所が多く。Many businesses in the laundry industry operate on a relatively small scale.
完全な機械化・自動化は望むべくもない。そのため、す
べての工程において極力省力化を図る必要がある。上記
(2)と(3)の問題は、撹拌を十分に行うことで加熱
を必要とせずに解決され得る。上記(4)の問題点は、
使用するα化澱粉が沈着物を発生させることなく冷水に
完全に溶けなければならず。Complete mechanization and automation cannot be expected. Therefore, it is necessary to save labor as much as possible in all processes. Problems (2) and (3) above can be solved by sufficient stirring without the need for heating. The problem with (4) above is that
The pregelatinized starch used must be completely soluble in cold water without forming deposits.
従来のα化澱粉ではそれは不可能であるため、未だ解決
され得ない。発生する沈着物は不均一な糊付けの原因と
なる。Since this is not possible with conventional pregelatinized starch, it has not yet been solved. The deposits that occur cause uneven gluing.
(発明が解決しようとする問題点)
本発明は上記従来の問題点を解決するものであり、その
目的の第一とするところは1次に示す性質を有する洗濯
糊用冷水易溶性粉末澱粉の製造方法を提供することにあ
る:
(1)加熱を必要としない冷水易溶性で即席性を有して
いること。(Problems to be Solved by the Invention) The present invention is intended to solve the above-mentioned conventional problems, and its first purpose is to provide a powdered starch that is easily soluble in cold water for laundry starch and has the following properties: The object of the present invention is to provide a manufacturing method: (1) It does not require heating, is readily soluble in cold water, and has instant properties.
(2)冷水溶解時に1節即な撹拌でも、また、一時に原
料を投入してもまま粉が生じない。また1分散性に優れ
ていること。(2) Even if the raw materials are added all at once during dissolution in cold water, no leftover powder will be produced, even if the material is stirred for one instant. It also has excellent monodispersibility.
(3)冷水溶解して放置したときに沈着物が発生しない
こと。(3) No deposits should be formed when dissolved in cold water and left to stand.
(4)洗濯糊に必須の以下の4条件を備えていること。(4) The laundry starch must meet the following four conditions.
すなわち。Namely.
イ)繊維に適当な固さと、風合いと弾力性をつける。b) Add appropriate hardness, texture and elasticity to the fibers.
TI)繊維につやと滑りをつげ、着心地をよくする。TI) Adds luster and slip to the fibers, making them more comfortable to wear.
ハ)衣類のアイロン整形をよ<シ、保形をたすける。そ
して。C) Help with ironing and shaping of clothing. and.
二)着用中に汚れが直接繊維の内部に滲透することを防
止し1次回に洗浄するとき、洪維につけた糊が洗い落と
されることにより繊維の汚れもよく落ちる。2) Prevents dirt from penetrating directly into the fibers during wear, and when washed for the first time, the glue applied to the fibers is washed away, and dirt from the fibers is also easily removed.
(問題点を解決するだめの手段)
本発明者らは、従来にない優れた性能をもつ冷水易溶性
の洗濯糊用澱粉を提供し・うる製造方法の開発に成功し
た6本発明の冷水易溶性の洗濯糊用澱粉の製造方法は、
澱粉に適量の硼酸、l酸塩。(Means for Solving the Problems) The present inventors have successfully developed a starch for use in laundry starch that is easily soluble in cold water and has excellent performance that has never existed before. The method for producing soluble laundry starch is as follows:
Appropriate amount of boric acid and chloride in starch.
重炭酸塩および炭酸塩の中から選ばれた1種または数種
を混合し、さらに必要に応じて、その他の酸類を加え、
得られた混合物のpHが3〜7.水分10〜30%の条
件下において、攪拌、移送、加熱および給水装置を一体
的に有する。連続式高圧、加圧、加熱装置内で、少な(
とも100°C以−トに加熱処理し、この加圧下の混合
物を、大気に放出することによって、澱粉粒を充分に膨
化せしめたのち。One or more selected from bicarbonates and carbonates are mixed, and if necessary, other acids are added,
The pH of the resulting mixture is 3-7. It has integrated stirring, transfer, heating, and water supply equipment under conditions of 10 to 30% moisture. In continuous high pressure, pressurization, and heating equipment,
Both were heated to 100°C or higher, and the mixture under pressure was released into the atmosphere to sufficiently expand the starch granules.
適当な粒子に粉砕することを特徴とし、そのことにより
目的が達成される。It is characterized by grinding into suitable particles, thereby achieving the purpose.
使用する澱粉は、コーンスターチ、ワキシーコーンスタ
ーチ、馬鈴薯澱粉、甘藷澱粉、小麦澱粉。The starches used are corn starch, waxy corn starch, potato starch, sweet potato starch, and wheat starch.
ダビオカスターチなど工業的に生産される澱粉であれば
何れを用いてもよい。さらに、各種天然澱粉を化学的に
化工された澱粉6例えば、酸処理澱粉などの軽度加水分
解澱粉、酸化澱粉、各種澱粉エステル、各種澱粉エステ
ルなども、ここでいう澱粉の定義に包含される。実用的
には、最も大量生産され2価格が安定しているコーンス
ターチが好ましい。澱粉に添加する物質は硼酸、硼酸塩
類としては硼砂2重炭酸塩としては重炭酸ソーダ。Any industrially produced starch such as davio castarch may be used. Furthermore, starches 6 that are chemically modified from various natural starches, such as mildly hydrolyzed starches such as acid-treated starches, oxidized starches, various starch esters, and various starch esters are also included in the definition of starch herein. Practically speaking, corn starch is preferred because it is produced in the largest quantity and has a stable price. The substance added to starch is boric acid, and the boric acid salt is borax bicarbonate, which is soda bicarbonate.
炭酸塩としては炭酸ソーダが適している。その他の酸類
としては、硫酸、燐酸などの無機酸および各種の有機酸
を用いることができる。添加する物質は、微粉砕されて
いる場合はそのまま澱粉に均質にl昆合することができ
、これらが、殿1分に1上べで。Soda carbonate is suitable as the carbonate. As other acids, inorganic acids such as sulfuric acid and phosphoric acid and various organic acids can be used. If the substances to be added are finely ground, they can be homogeneously mixed with the starch as is, and these can be added to the starch at a rate of 1/1 minute.
その粒度が大きい場合は、粉砕機で微粉砕してから澱粉
と均質に混合する。kン粉と均質に混合してから粉砕機
で粉砕することが混合の均一性が高まるという意味で好
ましい。If its particle size is large, it is finely ground in a grinder and then mixed homogeneously with starch. It is preferable to homogeneously mix it with the starch flour and then crush it with a crusher because this increases the uniformity of the mixture.
また使用量の少ない場合や、S状品の場合は適当な溶液
として、加圧、加熱装置の給水装置から添加して、加熱
される以前に、装置内で混合することもできる。In addition, if the amount used is small or if the product is S-shaped, it can be added as a suitable solution from the water supply device of the pressurizing and heating device and mixed in the device before being heated.
この場合の各添加物の使用量は、添加物の性質によって
差がある。In this case, the amount of each additive used varies depending on the nature of the additive.
例えば硼酸と重炭酸ソーダとを用いる場合では。For example, when using boric acid and bicarbonate of soda.
硼酸3〜10%2重炭酸ソーダ0.1〜0.5%である
。Boric acid 3-10%, bicarbonate of soda 0.1-0.5%.
硼酸と硼砂を用いる時は、硼酸3〜10%、硼砂0.1
〜1.5%である。硼酸も硼酸塩をも用いないときは1
重炭酸ソーダまたは炭酸ソーダを0.1〜0.5%用い
る。さらに後述する如<pHを調整するために、必要に
より、酸類を適量追加する。添加物総量として、12%
以下がよい。When using boric acid and borax, boric acid 3-10%, borax 0.1%
~1.5%. 1 when neither boric acid nor borate is used
Soda bicarbonate or soda carbonate is used at 0.1-0.5%. Further, as described below, an appropriate amount of acids is added as necessary to adjust the pH. 12% as total amount of additives
The following is good.
このように1本発明による製品の使用目的に応じてこれ
らから選択して用いる。In this way, one can be selected and used from these depending on the purpose of use of the product according to the present invention.
次に重要なことは、澱粉にこれら添加物を混合して得た
混合物のpHである。混合物の一部をとり。The next important thing is the pH of the mixture obtained by mixing these additives with starch. Take some of the mixture.
2倍量の水に懸濁させて、 pHを測定する。そのpH
の範囲は3〜7の範囲でなければならない、好ましくは
4.5〜6.5のpH範囲がよい、添加物混合後のpH
が前記の範囲を逸脱すると1本発明の目的とする洗濯糊
用澱粉の性能を有しなくなる。特に。Suspend in twice the amount of water and measure the pH. Its pH
should be in the range 3 to 7, preferably in the pH range 4.5 to 6.5, after mixing the additives.
If it deviates from the above-mentioned range, the starch for laundry paste will not have the performance as the object of the present invention. especially.
冷水溶解時の分散性が悪くまま粉ができやすくなる0強
い攪拌で溶解させても放置時に沈着物ができて、不均一
な糊付けになる。p)lが上記範囲を越えて高くなり過
ぎ、特に8以上になると、二輪式エクストリユーダーな
どによる連続高圧、加圧。Dispersibility when dissolving in cold water is poor and particles tend to form. Even if dissolved with strong stirring, deposits are formed when left to stand, resulting in uneven gluing. p) If l becomes too high beyond the above range, especially 8 or more, apply continuous high pressure or pressurization using a two-wheel extruder, etc.
加熱処理のときに2着色(茶−褐一黒)が激しく洗濯糊
としては使用できないものとなる。During the heat treatment, the two colors (brown-brown and black) are intense, making it unusable as a laundry paste.
添加物を混合した澱粉を次に2軸エクストリユーダーな
どを用いて加熱・加圧処理を行うが、該処理時の水分が
10〜30重量%の範囲内にあることが本発明にとり重
要な要素である。水分の調整方法には特に制限はない。The starch mixed with additives is then subjected to heat and pressure treatment using a twin-screw extruder, etc., but it is important for the present invention that the moisture content during this treatment is within the range of 10 to 30% by weight. is an element. There are no particular restrictions on the method of adjusting moisture.
水分が30重量%以上になると後述する膨化作用がなく
なり、出来上がった製品の冷水溶解性が悪くなる。より
好ましい水分量は10重量%から20重量%の範囲であ
る。When the water content exceeds 30% by weight, the swelling effect described below disappears, and the solubility of the finished product in cold water deteriorates. A more preferable water content is in the range of 10% to 20% by weight.
添加物混合澱粉の加熱・加圧処理に用いられる2軸のエ
クストリユーダーはプラスチック業界。The two-shaft extruder used for heat and pressure treatment of additive-mixed starch is used in the plastics industry.
食品業界に多用されているものでよく、特別規格である
必要はない。2軸のエクストリユーダーは。It may be one that is widely used in the food industry and does not need to be of any special standard. A two-axis extruder.
本発明においては、もっばら同方向回転型を用いたが異
方向回転型でも特に本発明を制約するものではない。先
端部圧力が少なくとも、 100kg/c+jG以上
、 200kg/aJGまで加圧できることが好ましい
。このエクストリユーダー処理により、供給原料素材が
充分にかつ適度にクツキングされて充分な澱粉粒子の膨
化が行われ、かつ生成物を粉砕して検鏡したときに微細
な針状結晶様物質が観察され、それを冷水に溶解したと
き微気泡が出現したとき最も本発明の目的に沿う洗濯糊
用澱粉が得られる。生成物の粉砕片を検鏡したとき、硝
子状の塊が観察される場合には9本発明の目的は達成さ
れない0本発明者らは硼酸、硼酸塩、炭酸塩2重炭酸塩
、その他の酸類などの薬剤と澱粉との混合処理、混合澱
粉の2軸エクストリユーダーなどによる加熱・加圧・膨
化処理、および澱粉膨化物の粉砕処理の組合せを研究す
ることにより本発明を完成させた0本発明方法により得
られる冷水易溶性の洗濯糊用澱粉は従来の製造方法によ
る製品と比較して、性能が優れていると同時に、製造コ
ストの軽減が行われ、産業上極めて有用である。In the present invention, although a co-rotating type is used, the present invention is not particularly limited to a different-direction rotating type. It is preferable that the pressure at the tip can be increased to at least 100 kg/c+jG and up to 200 kg/aJG. This extruder treatment ensures that the feedstock material is sufficiently and moderately packed to achieve sufficient starch particle expansion, and that fine needle-like crystal-like substances are observed when the product is crushed and examined under a microscope. When microbubbles appear when the starch is dissolved in cold water, the starch for laundry glue that best meets the purpose of the present invention can be obtained. When glass-like lumps are observed when the crushed pieces of the product are examined under a microscope, the object of the present invention will not be achieved9. The present invention was completed by researching the combination of mixing treatment of chemicals such as acids and starch, heating/pressure/swelling treatment of mixed starch using a twin-screw extruder, and pulverization of the puffed starch. The starch for laundry paste that is easily soluble in cold water obtained by the method of the present invention has superior performance and reduced production costs as compared to products produced by conventional production methods, and is extremely useful industrially.
なお1本発明により得られた冷水易溶性澱粉は次の如き
特長がある。Note that the cold water easily soluble starch obtained by the present invention has the following features.
■冷水に添加したときに、まま粉にならず、充分に均一
な分散液となり、長時間安定であり、沈着物は殆ど出な
い。■When added to cold water, it does not turn into powder, but forms a sufficiently uniform dispersion, is stable for a long time, and produces almost no deposits.
■この分散液の粘度は、従来のロール加熱・乾燥方式の
α化澱粉に比較して、約1/10位の低粘度でさらにこ
のものは、加熱しても粘度の変化がない。(2) The viscosity of this dispersion is about 1/10 lower than that of pregelatinized starch produced by conventional roll heating and drying methods, and the viscosity of this dispersion does not change even when heated.
■接着力も強く、適当な濃度の溶液にすることにより、
接着剤として用いることも勿論可能である。■The adhesive strength is also strong, and by making the solution at an appropriate concentration,
Of course, it can also be used as an adhesive.
■工程が簡単であり、乾燥の工程がなく、生産コストが
安い。したがって2本当は、洗濯用糊料のみならず、他
の従来のα化澱粉あるいは加工澱粉の用途にも利用でき
るものであり、新しい加工澱粉の製造法であるといえる
。■The process is simple, there is no drying process, and the production cost is low. Therefore, it can be said that the 2-layer method can be used not only as a laundry thickener but also for other conventional pregelatinized starches or modified starches, and is a new method for producing modified starches.
従来のロール加熱方式によるα化澱粉の製造工程と1本
発明による冷水易溶性澱粉の製造工程を示すと次の通り
になる。The manufacturing process of pregelatinized starch using the conventional roll heating method and the manufacturing process of cold water easily soluble starch according to the present invention are as follows.
(以下余白)
従来法は、R扮スラリーを直接原料とすることができる
が1本発明の方法では、一度乾燥した澱粉を用いなけれ
ばならない。(Left below) In the conventional method, the R starch slurry can be used directly as a raw material, but in the method of the present invention, starch that has been dried must be used.
しかし従来法では、加熱糊化処理後に乾燥工程を必要と
する。However, the conventional method requires a drying step after the heat gelatinization treatment.
この両者の乾燥費の一例を比較すると、従来のホットロ
ーラーなどによる加熱糊化後の乾燥は。Comparing an example of the drying costs of these two methods, drying after heating and gelatinization using a conventional hot roller etc.
製品kg当たり約25円を要するのに対し1本発明の乾
燥澱粉調整のための乾燥費(気流乾燥)はkg当たり約
6円である。The drying cost (airflow drying) for preparing dried starch according to the present invention is about 6 yen per kg, whereas it costs about 25 yen per kg of the product.
この乾燥費は、原料澱粉の価格に対して、それぞれ約2
7〜28%および6〜7%となる。This drying cost is approximately 2% of the price of raw starch.
7-28% and 6-7%.
他の運転費(電力費など)は1両者の工程に大きな差が
ない。従って9製造コストとじては、従来法よりも、か
なり安くなっている。There are no major differences in other operating costs (electricity costs, etc.) between the two processes. Therefore, the manufacturing cost is considerably lower than that of the conventional method.
本発明の方法で、製造した製品は、従来法に比して、冷
水易溶性である特長が大きい反面、 inn調製品発塵
性が高い欠点がある。この欠点は、0.5〜2%の油類
を噴霧混合することで、容易に防止でき、かつ冷水易溶
性2分散性に何らがの悪影ツを与えないことを見出した
。好ましくは、流動パラフィンを粉体混合機中で、噴霧
混合するのが良い。製品の使用目的によっては1食用油
を用いても良い。The product produced by the method of the present invention has the advantage that it is easily soluble in cold water compared to the conventional method, but has the disadvantage that the inn preparation has a high dust generation property. It has been found that this drawback can be easily prevented by spray-mixing 0.5 to 2% of oils, and that it does not have any negative effect on the easily cold water-soluble bidispersibility. Preferably, liquid paraffin is mixed by spraying in a powder mixer. Depending on the intended use of the product, one edible oil may be used.
J口屯−例−↓
コーンスターチ(三和澱粉工業株式会社製)2kgに硼
酸(IJ、 S、 Borax & CheIl、 C
orp、製 粉末状) 500g、!:、硼砂(前記
US社製 A−Fine) 25gを添加したいこれを
粉砕機にかけ(細用ミクロン領製AP−1型)にかけて
均一混合物を得た。コーンスターチをさらに8 kg追
加し、よく混合した。J Koutun - Example - ↓ 2 kg of cornstarch (manufactured by Sanwa Starch Industries Co., Ltd.) and boric acid (IJ, S, Borax & CheIl, C
orp, powder form) 500g,! 25 g of borax (A-Fine, manufactured by US Corporation) was added thereto, and the mixture was passed through a pulverizer (Model AP-1, manufactured by Hoiyo Micron Ryōryō) to obtain a homogeneous mixture. An additional 8 kg of cornstarch was added and mixed well.
この添加物混合澱粉のpl(は、5.7であった。この
pi(はこの添加物混合澱粉に2倍量の水を加え、得ら
れた懸濁水のpHを測定したものである。また。The pl () of this additive-mixed starch was 5.7. This pi () was measured by adding twice the amount of water to this additive-mixed starch and measuring the pH of the suspension water obtained. .
処理後のpHは表に示すように、7.0に上昇していた
。この水分は12.5%であった。この添加物混合澱粉
を次いで2軸エクストリユーダー(株式会社幸和工業製
のに11i1−45−15型)にかけた。このエクスト
リユーダーのスクリューパターンは通常のスクリューの
先端部にフライカットリバーススクリューおよびニーデ
ィングディスクを各々ペアーでとりつけたものであった
。グイ開口部は一つでありその直径ば5■であった。原
料の供給は毎分500gで、運転開始時のみ水を供給し
、その後は水の添加は行わなかった。スクリューの回転
は毎分290回転であった。エクストリプ、−ダーの温
度条件はスクリューの供給口付近が30℃、中位部が8
0”c。As shown in the table, the pH after treatment had increased to 7.0. This water content was 12.5%. This additive-mixed starch was then subjected to a twin-screw extruder (model 11i1-45-15 manufactured by Kowa Kogyo Co., Ltd.). The screw pattern of this extruder was a pair of fly-cut reverse screws and a kneading disk attached to the tip of a normal screw. There was one opening, and its diameter was 5 mm. Raw materials were supplied at a rate of 500 g per minute, water was supplied only at the start of operation, and no water was added thereafter. The rotation of the screw was 290 revolutions per minute. The temperature conditions for Extrap and -der are 30℃ near the screw supply port and 8℃ in the middle part.
0”c.
先端部が160℃、そしてグイ部が125℃であった。The temperature at the tip was 160°C, and the temperature at the goo was 125°C.
先端部の圧力は15kg/efflGであった。グイ部
よりストランド状で排出される膨化澱粉は1回転刃(6
枚方1700回転)でホットカット・され、これがただ
ちに空気輸送されて流動層冷却装置に送られ常温に冷却
された。これを粉砕し、 20メツシユの篩に通したう
得られた粉砕物を以下の洗濯糊用澱粉適性試験のための
試料とした。この試料の粒度分布は、20メソシユから
60メンシユの間が全体の35.6重量%、60メツ
シュから150メフシユの間が3967重璽%重曾15
0メフシノ、スルーが24.7重量%であった。見掛は
比重は約o、15であった。冷水可溶性の洗濯糊用澱粉
の適性試験は次の方法で行なった。The pressure at the tip was 15 kg/efflG. The expanded starch discharged in the form of strands from the goo is produced by a single rotating blade (6
It was hot-cut at a speed of 1,700 revolutions (1,700 rpm), and immediately transported by air to a fluidized bed cooling device where it was cooled to room temperature. This was crushed and passed through a 20-mesh sieve, and the resulting crushed product was used as a sample for the following starch suitability test for laundry paste. The particle size distribution of this sample was as follows: 20 mesh to 60 mesh was 35.6% of the total weight, and 60 mesh to 150 mesh was 3967% by weight.
The amount of through was 24.7% by weight. The apparent specific gravity was approximately 0.15. The suitability test of cold water soluble starch for laundry glue was carried out in the following manner.
a、粘度
i)冷時粘度
1.500m6容ステンレス製ビーカーに30℃の純水
450ra 1を入れる。a. Viscosity i) Viscosity when cold: 1.Pour 450ra 1 of pure water at 30°C into a 500m6 stainless steel beaker.
2、上皿天秤にて試料を25g(無水換算)採取し、ビ
ーカー中によく攪拌しながら少量ずつ投入溶解し、さら
に水でうすめて全量を500 gにする。2. Collect 25g (anhydrous equivalent) of the sample using a top balance, pour it into a beaker little by little and dissolve while stirring well, and further dilute with water to make a total amount of 500g.
3、この後室温にて30分間攪拌を行う。攪拌は550
rpa+〜600rpmとする。3. After this, stir at room temperature for 30 minutes. Stirring is 550
rpa+ to 600 rpm.
4.30℃でB型粘度針で測定する。4. Measure with a type B viscosity needle at 30°C.
ii)加熱粘度
1、冷時粘度測定後の液を激しく沸騰している湯煎鍋中
でよく攪拌しながら90℃まで上昇させる。ii) The liquid after heating viscosity 1 and cold viscosity measurement is heated to 90° C. while stirring well in a hot water pot with vigorous boiling.
2.90℃になったら純水にて内容を500gとして流
水中で攪拌しながら冷却する。2. When the temperature reaches 90°C, add pure water to bring the content to 500g, and cool while stirring in running water.
3.30℃でB型粘度計で測定する。3. Measure with a B-type viscometer at 30°C.
加熱粘度が冷時粘度より高い場合は、製品中に膨潤不充
分な、澱粉粒が残存しており、このものが加熱により、
粘性を示すように変化したと考えられるので、冷水に溶
解して用いたときは、このものが糊付け・アイロンかけ
後の不均一状態の原因となる。If the heated viscosity is higher than the cold viscosity, there are starch granules remaining in the product that are insufficiently swollen, and these are
It is thought that it has changed to exhibit viscosity, so when it is dissolved in cold water and used, this will cause an uneven state after gluing or ironing.
b、沈着物の量 1、上皿天秤にて試料を4g(現物)採取する。b. Amount of deposits 1. Collect 4g (actual) sample using a top balance.
2.100mAのビーカーに水を入れ、よく攪拌しなが
ら試料を溶解する。2. Pour water into a 100 mA beaker and dissolve the sample while stirring well.
3、溶解した液を200m6メスシリンダーに入れ、全
量を200m1になるように加水する。3.Pour the dissolved solution into a 200m6 measuring cylinder and add water to make the total volume 200ml.
4、室温で3時間放置し、3時間後、その沈着物の容積
(mA’)を読みとる。4. Leave at room temperature for 3 hours, and after 3 hours, read the volume (mA') of the deposit.
この沈着物が生成することは、液中に糊の不均一粒子が
存在することを意味し、洗濯糊用澱粉としては、好まし
くない。The formation of this deposit means the presence of non-uniform particles of starch in the liquid, which is not desirable as a starch for laundry glue.
C1見掛は比重
1.20On+6のプラスチック製メスシリンダーに試
料を200mj!まで静かに入れ、その時の中味重量を
測定して、粗の見掛は比重を算出する。C1 The apparent specific gravity is 200mj in a plastic graduated cylinder with a specific gravity of 1.20On+6! Pour the contents gently until it reaches 100 degrees, measure the weight of the contents, and calculate the rough appearance and specific gravity.
2、メスシリンダーを充分にタッピングしたときの容積
を測定し、その値から、密の見掛は比重を算出する。2. Measure the volume when tapping the graduated cylinder sufficiently, and calculate the apparent density and specific gravity from that value.
見掛は比重の極度に大きい場合は溶解性の悪い場合が多
い。If the apparent specific gravity is extremely high, solubility is often poor.
d、pH
試料を無水換算で3g採取し、あらかじめ70〜80n
+ 1の純水をいれた100m l容ビーカーに攪拌し
ながら少量づつ投入後全体を100gとして、 PHツ
メ−−で測定する。d, pH Collect 3g of the sample on an anhydrous basis, and
Pour the mixture into a 100 ml beaker containing +1 pure water little by little while stirring, then measure the total amount using a PH meter.
製品の使用目的に対応して、適当なpH範囲を定める。Determine an appropriate pH range depending on the intended use of the product.
e、糊付はテスト(洗濯糊適性テスト)試料を無水換算
で4gを採り、30℃の水に溶解して、全jt200m
lの2%糊液をつくる。水に浸したさらし布をよ(しぼ
り、この糊液に充分浸漬し、余分の糊液を振り切ってか
ら乾燥する。生乾きの状態でアイロン掛けして、その糊
付は状態・光沢性などを肉眼または拡大鏡、さらには沃
素溶液を滴下して顕微鏡で観察する。e. For gluing, take 4g of the test sample (washing starch suitability test) in terms of dryness, dissolve it in water at 30°C, and make a total of 200m of water.
Make 1 liter of 2% starch solution. Dip a bleached cloth soaked in water (squeeze) thoroughly into this starch solution, shake off the excess starch solution, and then dry. Iron the half-dry state and check the condition and glossiness of the glue with the naked eye. Alternatively, use a magnifying glass or even a drop of iodine solution and observe under a microscope.
比較■
コーンスターチのみを用い硼酸と硼砂を用いなかったこ
と以外はすべて実施例1と同様に加圧。Comparison ■ Pressurization was carried out in the same manner as in Example 1 except that only cornstarch was used and boric acid and borax were not used.
加熱処理を施したものである。 以上の諸試験により得
られた洗濯糊用澱粉としての特性を従来から生産されて
いるアル°2アコーンスターチ(三和澱粉工業株式会社
製)および比較例と比較すると次表のようになる。It is heat treated. The properties of starch for laundry paste obtained through the above tests are compared with conventionally produced Al°2 Acorn Starch (manufactured by Sanwa Starch Industries Co., Ltd.) and comparative examples, as shown in the following table.
(以下余白)
従来のα化コーンスターチは水に溶解して検鏡したとき
0.1〜0 、2 mmの膨潤澱粉粒の切片が認められ
、完全な)懸濁状態になっていない。そのため。(Left below) When conventional pregelatinized cornstarch is dissolved in water and examined under a microscope, sections of swollen starch granules of 0.1 to 0.2 mm are observed, and it is not completely suspended. Therefore.
30℃の水に溶解して粘度を測定すれば280cpであ
るが、 90℃の熱湯で溶解してから30℃に冷却して
粘度を測定すれば820C[)であった。冷水溶解した
糊の静置時の沈着物が40%もあった。この従来のα化
コーンスターチは完全に糊化t7ていないので。When dissolved in water at 30°C and measured, the viscosity was 280 cp, but when dissolved in hot water at 90°C and then cooled to 30°C, the viscosity was measured to be 820 C[). As much as 40% of the glue dissolved in cold water was deposited when left standing. This conventional pregelatinized cornstarch is not completely gelatinized.
まだ熱により溶解増粘する余地を残していることを示し
ている。This shows that there is still room for melting and thickening due to heat.
他方、実施例1で製造j7た加工澱粉ば水に溶解して検
鏡したとき、150侑率で1ま原形が完全にくずれて、
如何なる形状も認められない。冷時粘度も加熱粘度も変
わらなかつ六二。しかも、沈着物も全く発生しない。こ
れはほぼ完全に糊化していることを示している。しかも
、粘度は従来のα化コーンスターチより極端に低い。こ
れは2軸エクストリユーダーによる加熱・加圧・膨化処
理により澱粉分子が大きな機械的剪断をうけていること
。On the other hand, when the modified starch produced in Example 1 was dissolved in water and examined under a microscope, its original shape completely collapsed at a rate of 150 mm.
No shape is allowed. The viscosity when cold and when heated is 62. Furthermore, no deposits are generated. This shows that it is almost completely gelatinized. Moreover, the viscosity is extremely lower than that of conventional pregelatinized cornstarch. This means that the starch molecules are subjected to large mechanical shearing due to the heating, pressurizing, and swelling treatment performed by the twin-screw extruder.
すなわち、澱粉分子は寸断され小さくなっていることを
示している。このことば、洗濯糊の繊維への浸透性にお
いて有利であり、均一に付着する所以だと考えられる。In other words, the starch molecules are fragmented and become smaller. This word is advantageous in terms of permeability of laundry starch into fibers, and is thought to be the reason why it adheres uniformly.
さらに3本発明の加工澱粉の最も大きい特徴は。Furthermore, the three most important features of the processed starch of the present invention are:
冷水溶解時にまま粉にならずに分散性が優れ、容易に溶
解する所にある。従来のα化コーンスターチおよび比較
例では溶解時に相当激しく水を攪拌しながら、極く少量
づつ試料を添加し7なりれば。It has excellent dispersibility without turning into powder when dissolved in cold water, and dissolves easily. In the case of conventional pregelatinized cornstarch and comparative examples, the sample was added in very small amounts at a time of 7 while stirring the water quite vigorously during dissolution.
まま粉が生じる。−互生じたまま粉は、その後。Leaves will form. - After that, the powder will remain as it is.
少々の攪拌では溶解しない。It will not dissolve with slight stirring.
n1?一
実施例1のコーンスターチの代わりに馬鈴薯6粉を用い
た。実施例1で得られた澱粉と同しく。n1? In place of the cornstarch in Example 1, 6 potato flour was used. Same as starch obtained in Example 1.
すべての洗濯糊適性の良好な、冷水易溶性の洗濯糊用澱
粉が得られた。A starch for laundry paste, which was easily soluble in cold water and had good suitability as a laundry paste, was obtained.
実JF医主
実施例1のコーンスターチの代わりに小麦澱粉を用いた
。実施例1で得られた澱粉と同じく、すべての洗濯糊適
性の良好な冷水易溶性の洗濯糊用澱粉が得られた。Wheat starch was used instead of cornstarch in Example 1. As with the starch obtained in Example 1, a starch for laundry paste that was easily soluble in cold water and had good suitability as a laundry paste was obtained.
スJJL先
コーンスターチ10kgに硼酸500 gと重炭酸ソー
ダ15gをよく混合した。この時のpHは6.0.水分
は12.8%であった。このものについて以下はすべて
、実施例1と同様にして加工澱粉の調製を行った。500 g of boric acid and 15 g of bicarbonate of soda were thoroughly mixed with 10 kg of corn starch. The pH at this time was 6.0. Moisture was 12.8%. Regarding this product, processed starch was prepared in the same manner as in Example 1.
実施例1の澱粉と同じく、すべての洗濯糊適性の良好な
、冷水易溶性の洗濯糊用澱粉が得られた。As with the starch of Example 1, a starch for laundry paste, which had good suitability as a laundry paste and was easily soluble in cold water, was obtained.
大嵐■エ コーンスターチ10kgに硼砂200gをよく混合し。Big storm Mix 10kg of cornstarch and 200g of borax thoroughly.
さらに10%の硫酸を、500■lよく混合しなから噴
霧混合した。この時のpHは5.5.水分は13.2%
であった。このものについて以下は、すべて、実施例1
と同様にして澱粉の調製を行った。実施例1の澱粉と同
じく、すべての洗濯糊適性の良好な。Further, 500 l of 10% sulfuric acid was mixed well and then sprayed. The pH at this time was 5.5. Moisture is 13.2%
Met. The following is all about this thing, Example 1
Starch was prepared in the same manner. Like the starch of Example 1, all the laundry starch properties were good.
冷水易溶性の洗濯糊用澱粉が得られた。A starch for laundry paste which is easily soluble in cold water was obtained.
去立尉旦
コーンスターチ10kgに食品添加物の重炭酸ソーダ3
0gおよび同じく食品添加物のクエン酸20gを粉砕器
を通しながら充分に混合した。この時のpiは6.l、
水分は12.7%であった。このものについて以下は実
施例1と同様にして、澱粉の調製を行った。10 kg of Yudan corn starch and 3 parts of bicarbonate of soda as a food additive
0 g and 20 g of citric acid, which is also a food additive, were thoroughly mixed through a pulverizer. The pi at this time is 6. l,
Moisture was 12.7%. Regarding this product, starch was prepared in the same manner as in Example 1.
本実施例による加工澱粉は、冷水易溶性の低粘性粘稠剤
としての有効な適性を有し1食品用の粘稠剤として良好
である。The modified starch according to this example has an effective suitability as a low-viscosity thickening agent that is easily soluble in cold water, and is good as a thickening agent for food products.
ス皇■1
実施例4により得られた冷水易溶性加工澱粉10眩を充
分に混合攪拌しながら約60℃に加熱した流動パラフィ
ン100gを噴霧混合した。1. 10 g of the cold water easily soluble modified starch obtained in Example 4 was thoroughly mixed and stirred, and 100 g of liquid paraffin heated to about 60° C. was spray-mixed.
本加工澱粉は実施例1〜6により製造された澱粉が若干
の発塵性を有するのに対して発塵性は殆どなく、使用時
に便宜である。同時に実施例1〜6の加工澱粉の本発明
の有効性は、何ら阻害されていない。Unlike the starches produced in Examples 1 to 6, which generate some dust, this modified starch hardly generates dust, and is convenient in use. At the same time, the effectiveness of the processed starches of Examples 1 to 6 according to the present invention was not impaired in any way.
スJJLL
実施例6に得られた冷水易溶性加工澱粉10kgをはげ
しく混合攪拌しながら、コーンサラダオイルを100
g噴霧混合した。While vigorously mixing and stirring 10 kg of the cold water easily soluble modified starch obtained in Example 6, add 100 kg of corn salad oil.
g Spray mixed.
本加工澱粉は、実施例6により製造された澱粉が若干の
発塵性を有するのに対して9発塵性は殆どなく、使用時
に便宜である。While the starch produced in Example 6 has a slight dust-generating property, this modified starch has almost no dust-generating property and is convenient in use.
同時に実施例6の加工澱粉の本発明の有効性は何ら阻害
されていない。At the same time, the effectiveness of the processed starch of Example 6 according to the present invention is not impaired in any way.
(発明の効果)
本発明方法によれば、このように、硼酸・硼砂・炭酸塩
・重炭酸塩・その他の酸類等の添加物と原料澱粉との混
合処理、添加物混合澱粉のpH,水分を厳密に規制した
のち2軸エクストリニーダ−などによる連続式高圧・加
圧・加熱・膨化処理、および澱粉膨化物の粉砕処理の巧
みな組合せにより。(Effects of the Invention) According to the method of the present invention, as described above, the mixing treatment of additives such as boric acid, borax, carbonates, bicarbonates, and other acids with raw starch, the pH of the additive-mixed starch, and the water content After strictly regulating the process, a skillful combination of continuous high pressure, pressurization, heating, and swelling treatment using a two-screw extri-kneader, etc., and pulverization of the starch puffed material are used.
■簡単な攪拌によりまま粉を生じることなく冷水に容易
に溶ける分散性に優れた澱粉:■冷水に溶解後、放置し
ておいても沈着物が生じない澱粉;そして■繊維に適度
の固さと風合いと弾力性とつやと滑りを付与し2着心地
をよくすると同時に。■ A starch with excellent dispersibility that easily dissolves in cold water without forming a lump by simple stirring; ■ A starch that does not form deposits even if left standing after being dissolved in cold water; and ■ A starch that has an appropriate hardness on the fiber It provides texture, elasticity, shine, and slippage, making it comfortable to wear.
アイロン整形をよくし保形を助け、しかも繊維の汚れを
洗濯により筋単に落としうる澱粉が得られる。なお9本
発明の製造法は、上記各種条件の組合せを選択すること
により2種々の用途に応用できる特性を有した冷水易溶
性の加工澱粉を製造することができる。しかも、製造工
程が従来法に比較して著しく簡便・容易であり、製造コ
ストも従来法に比較して著しく低い。It is possible to obtain a starch that improves iron shaping and helps shape retention, and also allows stains on fibers to be easily removed by washing. By selecting a combination of the various conditions described above, the production method of the present invention can produce a processed starch that is easily soluble in cold water and has characteristics that can be applied to a variety of uses. Moreover, the manufacturing process is significantly simpler and easier than conventional methods, and the manufacturing cost is also significantly lower than conventional methods.
以上that's all
Claims (1)
の中から選ばれた1種または数種を混合し、さらに必要
に応じて、その他の酸類を加え、得られた混合物のpH
が3〜7、水分10〜30%の条件下において、攪拌、
移送、加熱および給水装置を一体的に有する、連続式高
圧、加圧、加熱装置内で、少なくとも100℃以上に加
熱処理し、この加圧下の混合物を、大気に放出すること
によって、澱粉粒を充分に膨化せしめたのち、適当な粒
子に粉砕することを特徴とする、冷水易溶性加工澱粉の
製造方法。 2、前記硼酸塩としては硼砂、重炭酸塩としては重炭酸
ソーダ、炭酸塩としては炭酸ソーダ、である特許請求の
範囲第1項に記載の製造方法。 3、前記添加物の総量は澱粉100重量部に対して、0
.1から30重量部である特許請求の範囲第1項に記載
の製造方法。 4、前記連続式高圧、加圧、加熱装置としては2軸のエ
クストリユーダーが用いられる特許請求の範囲第1項に
記載の製造方法。 5、特許請求の範囲第1項から第4項に記載の方法によ
り製造された粉末状の冷水易溶性澱粉に0.5〜3%の
油類を噴霧混合することによる冷水易溶性加工澱粉の製
造方法。[Claims] 1. Mix an appropriate amount of one or more selected from boric acid, borates, bicarbonates, and carbonates with starch, and further add other acids as necessary; pH of the resulting mixture
is 3 to 7 and the moisture content is 10 to 30%, stirring,
The starch granules are heated to at least 100°C in a continuous high-pressure, pressurized, and heated device that has integrated transfer, heating, and water supply devices, and the mixture under pressure is released into the atmosphere. A method for producing a processed starch that is readily soluble in cold water, which comprises sufficiently expanding the starch and then pulverizing it into suitable particles. 2. The manufacturing method according to claim 1, wherein the borate is borax, the bicarbonate is sodium bicarbonate, and the carbonate is soda carbonate. 3. The total amount of the additives is 0 per 100 parts by weight of starch.
.. The manufacturing method according to claim 1, wherein the amount is 1 to 30 parts by weight. 4. The manufacturing method according to claim 1, wherein a two-shaft extruder is used as the continuous high pressure, pressurization, and heating device. 5. Processed starch that is easily soluble in cold water by spray-mixing 0.5 to 3% of oil to the powdered starch that is easily soluble in cold water produced by the method described in claims 1 to 4. Production method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18809986A JPH0725801B2 (en) | 1986-08-11 | 1986-08-11 | Processed starch manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18809986A JPH0725801B2 (en) | 1986-08-11 | 1986-08-11 | Processed starch manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6343902A true JPS6343902A (en) | 1988-02-25 |
| JPH0725801B2 JPH0725801B2 (en) | 1995-03-22 |
Family
ID=16217682
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18809986A Expired - Fee Related JPH0725801B2 (en) | 1986-08-11 | 1986-08-11 | Processed starch manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0725801B2 (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5411218A (en) * | 1992-07-02 | 1995-05-02 | Daiwa Seiko, Inc. | Bearing type drag mechanism for fishing reel |
| US5601245A (en) * | 1993-03-26 | 1997-02-11 | Daiwa Seiko, Inc. | Brake system for use in double bearing type fishing reel |
| KR20000053946A (en) * | 2000-05-12 | 2000-09-05 | 문윤도 | Industrial dextrin And Method Of Preparing Thereof |
| US6164576A (en) * | 1998-06-26 | 2000-12-26 | Daiwa Seiko, Inc. | Reel for fishing which stably and easily performs fishing operations without imparting shock to fishing line |
| CN1074423C (en) * | 1997-04-11 | 2001-11-07 | 国内贸易部谷物油脂化学研究所 | Predextrinizing finishing starch and its preparing method |
| WO2003014217A1 (en) * | 2001-08-07 | 2003-02-20 | Eiko Yamaguchi | Biodegradable polymer blend |
| CN117652653A (en) * | 2022-08-31 | 2024-03-08 | 廊坊梅花生物技术开发有限公司 | Composite stabilizer containing xanthan gum and preparation method and application thereof |
| CN117700571A (en) * | 2023-12-19 | 2024-03-15 | 广东海洋大学 | Modified starch material with high thermal stability and preparation method thereof |
-
1986
- 1986-08-11 JP JP18809986A patent/JPH0725801B2/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5411218A (en) * | 1992-07-02 | 1995-05-02 | Daiwa Seiko, Inc. | Bearing type drag mechanism for fishing reel |
| US5601245A (en) * | 1993-03-26 | 1997-02-11 | Daiwa Seiko, Inc. | Brake system for use in double bearing type fishing reel |
| CN1074423C (en) * | 1997-04-11 | 2001-11-07 | 国内贸易部谷物油脂化学研究所 | Predextrinizing finishing starch and its preparing method |
| US6164576A (en) * | 1998-06-26 | 2000-12-26 | Daiwa Seiko, Inc. | Reel for fishing which stably and easily performs fishing operations without imparting shock to fishing line |
| KR20000053946A (en) * | 2000-05-12 | 2000-09-05 | 문윤도 | Industrial dextrin And Method Of Preparing Thereof |
| WO2003014217A1 (en) * | 2001-08-07 | 2003-02-20 | Eiko Yamaguchi | Biodegradable polymer blend |
| CN117652653A (en) * | 2022-08-31 | 2024-03-08 | 廊坊梅花生物技术开发有限公司 | Composite stabilizer containing xanthan gum and preparation method and application thereof |
| CN117700571A (en) * | 2023-12-19 | 2024-03-15 | 广东海洋大学 | Modified starch material with high thermal stability and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0725801B2 (en) | 1995-03-22 |
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