JPS6324865A - Granular paste and production thereof - Google Patents
Granular paste and production thereofInfo
- Publication number
- JPS6324865A JPS6324865A JP61168956A JP16895686A JPS6324865A JP S6324865 A JPS6324865 A JP S6324865A JP 61168956 A JP61168956 A JP 61168956A JP 16895686 A JP16895686 A JP 16895686A JP S6324865 A JPS6324865 A JP S6324865A
- Authority
- JP
- Japan
- Prior art keywords
- paste
- water
- granular
- powder
- soluble
- 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 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 239000002245 particle Substances 0.000 claims abstract description 31
- 239000000843 powder Substances 0.000 claims abstract description 23
- 239000004552 water soluble powder Substances 0.000 claims abstract description 22
- 238000005507 spraying Methods 0.000 claims abstract description 17
- 239000002994 raw material Substances 0.000 claims abstract description 14
- 238000001035 drying Methods 0.000 claims abstract description 8
- 239000008187 granular material Substances 0.000 claims abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 3
- 239000003381 stabilizer Substances 0.000 abstract description 3
- 239000000230 xanthan gum Substances 0.000 abstract description 2
- 235000010493 xanthan gum Nutrition 0.000 abstract description 2
- 229920001285 xanthan gum Polymers 0.000 abstract description 2
- 229940082509 xanthan gum Drugs 0.000 abstract description 2
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 abstract 1
- 235000013312 flour Nutrition 0.000 abstract 1
- 239000001863 hydroxypropyl cellulose Substances 0.000 abstract 1
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 abstract 1
- 239000003960 organic solvent Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 15
- 239000003292 glue Substances 0.000 description 13
- 230000015572 biosynthetic process Effects 0.000 description 10
- 239000011230 binding agent Substances 0.000 description 9
- 239000008213 purified water Substances 0.000 description 6
- 235000013339 cereals Nutrition 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 241000567769 Isurus oxyrinchus Species 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000001186 cumulative effect Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000004088 foaming agent Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000011163 secondary particle Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- -1 strings Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 description 1
- 244000215068 Acacia senegal Species 0.000 description 1
- 241000282816 Giraffa camelopardalis Species 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- 229920000084 Gum arabic Polymers 0.000 description 1
- 229920003114 HPC-L Polymers 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 244000046052 Phaseolus vulgaris Species 0.000 description 1
- 235000010627 Phaseolus vulgaris Nutrition 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 235000010489 acacia gum Nutrition 0.000 description 1
- 239000000205 acacia gum Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 235000021120 animal protein Nutrition 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000011978 dissolution method Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010419 fine particle Substances 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
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
- 235000010417 guar gum Nutrition 0.000 description 1
- 229960002154 guar gum Drugs 0.000 description 1
- 229920000591 gum Polymers 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000010981 methylcellulose Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 229940023462 paste product Drugs 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 description 1
- 235000021395 porridge Nutrition 0.000 description 1
- 239000011164 primary particle Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 235000010413 sodium alginate Nutrition 0.000 description 1
- 239000000661 sodium alginate Substances 0.000 description 1
- 229940005550 sodium alginate Drugs 0.000 description 1
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 239000003021 water soluble solvent Substances 0.000 description 1
Landscapes
- General Preparation And Processing Of Foods (AREA)
- Jellies, Jams, And Syrups (AREA)
- Cereal-Derived Products (AREA)
Abstract
Description
【発明の詳細な説明】
11且11
技術分野
本発明は、水に対して即溶性のある粒状糊料およびその
製造法に関する。Detailed Description of the Invention 11 and 11 Technical Field The present invention relates to a granular paste that is immediately soluble in water and a method for producing the same.
従来より水溶性粉末糊料(特に可食性のもの)は、分散
系の安定化、ゲル化、増粘、皮膜形成、テクスチャーの
向上等を目的とした安定剤としC1畜産加工品、水産加
工品等の食品業界において広く使用されているのみなら
ず、化粧品、綴紐、製紙、医薬品等の他の゛業界におい
ても広範m1にわたり使用されている。Traditionally, water-soluble powder pastes (especially edible ones) have been used as stabilizers for the purpose of stabilizing dispersion systems, gelling, thickening, forming films, improving texture, etc., and are used in C1 livestock processed products and marine processed products. It is widely used not only in the food industry, but also in other industries such as cosmetics, strings, paper manufacturing, and pharmaceuticals.
しかしながら、水溶性粉末糊料は、これを水に溶解させ
る際に通゛常の撹拌による溶解時に所謂ママコを形成す
るので、製品加工に使用する上で種々の問題点く糊料の
溶解に時間がかかる、糊料の高濃度溶液をつくることが
できない等)を抱えている。ここでママコとは、粉末糊
料を水に溶解させるに際し、水と接した粒子(接水粒子
)のみが膨潤して高粘−となるため、接水粒子に囲まれ
た内側の粉末と水との接触が著しく阻害されることによ
り生じる塊のことをいう。However, when water-soluble powder paste is dissolved in water, it forms a so-called lump when dissolved by ordinary stirring, so there are various problems when using it in product processing, and it takes time to dissolve the paste. (e.g., it takes a lot of water, the inability to make a highly concentrated solution of glue, etc.) Here, mamako means that when powdered glue is dissolved in water, only the particles that come into contact with water (particles in contact with water) swell and become highly viscous. This refers to a lump that occurs when contact with the substance is significantly inhibited.
九1且韮
このママコの形成′を防ぐため、例えば、粉末糊料を篩
分することによって微粒子および粗大粒子を除いて粒子
径をある程度均一にしで、糊料の溶解性を高めるという
方法が行われてきた。91. In order to prevent the formation of porridges, for example, a method of increasing the solubility of the paste is to sieve the powdered paste to remove fine particles and coarse particles and make the particle size uniform to some extent. It has been.
また、発泡剤や無機塩等を添加することによりママコの
形成を防ぐとともに糊料の溶解度を高めたり、あるいは
ママコを生じ易い粉末糊料については、この粉末をママ
コを生じにくい粉末糊料(ポリビニルアルコール等)で
コーティングすることによりママコの形成を防ぐととも
に溶解時間を短縮する方法も行われている。In addition, by adding foaming agents, inorganic salts, etc., it is possible to prevent the formation of mako and increase the solubility of the paste. Coating with alcohol, etc.) is also used to prevent the formation of mako and shorten the dissolution time.
しかしながら、上記で粉末糊料の粒子をある程度均一に
するという方法はママコ形成を防ぐための本質的な解決
策とはならず、また発泡剤や無機塩を添加−する方法は
これらを添加Jることにより糊液の粘度が低下するとい
う新たな問題を生じ、さらに粉末糊料を別のママコを生
じにくい糊料でコーティングする方法は、主成分(ママ
コを生じ易い糊料)の特性が阻害されたり、糊液粘度も
変動する等の問題点を抱えており、いずれにしてもママ
コの形成防止ないし消失法として効果的ではなかった。However, the above method of making the particles of the powdered glue uniform to some extent is not an essential solution to preventing the formation of lumps, and the method of adding foaming agents and inorganic salts does not provide a substantial solution to preventing the formation of bulges. As a result, a new problem arises in that the viscosity of the glue solution decreases.Furthermore, the method of coating the powdered glue with another glue that does not easily cause lumps may inhibit the properties of the main component (the glue that tends to cause lumps). However, this method has problems such as fluctuations in the viscosity of the glue, and in any case, it has not been effective as a method for preventing or eliminating the formation of lumps.
このよう5な問題点に対処すサク、本発明者らは、先に
水溶性粉末糊料の粒子間を結合剤(ただし、その5%水
水溶溶液粘度(20℃)は1000センチボイズ以上で
ある)で架橋ツ゛ることによって造粒されたものである
ことを特徴する粒状糊料、およびその製造法として流動
化された水溶性粉末糊料粒子に結合剤(ただし、その5
%水溶液の粘度(20℃)は1000センチボイズ以上
である)の水溶液を噴霧したのち乾燥して、水溶性粉末
糊料の粒子間を結合剤で架橋させてなる粒状物を得るこ
とを特徴とする方法を提案した(特Irl昭60−94
421号の明細書参照、以下「先願発明」という。)。To address these five problems, the present inventors first used a binder between the particles of a water-soluble powder paste (however, the viscosity of a 5% aqueous solution (at 20°C) was 1000 centivoise or more). ), and the manufacturing method thereof includes adding a binder to fluidized water-soluble powder paste particles (however, the 5
% aqueous solution (viscosity (at 20°C) is 1000 centiboise or more) is sprayed and then dried to obtain granules by crosslinking particles of water-soluble powder paste with a binder. proposed a method (Special Irl 1986-1994)
See the specification of No. 421, hereinafter referred to as the "prior invention". ).
11且IH
!−1
本発明は、上記粒状糊料を製造するにあたり、その製造
工程において、結合剤として水を使用しても先願発明と
同様の粒状糊料を得ることを見出して完成されたもので
ある。11 IH! -1 The present invention was completed by discovering that even when water is used as a binder in the production process of the above granular paste, the same granular paste as in the prior invention can be obtained. .
従って、本発明による粒状糊料は、水溶性粉末糊料に水
を噴霧することにより造粒された粒子からなるものであ
って、下記の性質を有すること、を特徴とするものであ
る。Therefore, the granular paste according to the present invention consists of particles granulated by spraying water on a water-soluble powder paste, and is characterized by having the following properties.
(イ) 12メツシュI(JIS規格)を実質的に全量
が通過し、100メツシュ篩(JIS規625)上に実
質的に令聞が残る粒面であること。(a) The grain surface must be such that substantially all of the grain passes through 12 mesh I (JIS standard) and a grain remains on a 100 mesh sieve (JIS standard 625).
(ロ) 見掛は比容積が、糊料粉末原料の兄liトは比
容積の少なくとも1.3倍であること。(b) The apparent specific volume of the paste powder raw material should be at least 1.3 times the specific volume.
また、本発明は、上記粒状糊料の製造法にも関する。The present invention also relates to a method for producing the above-mentioned granular paste.
すなわち、本発明による粒状糊料の製造法は、流動化さ
れた水溶性粉末糊料粒子に水を噴霧したのち乾燥して、
下記の性質を有する粒状物を得ること、を特徴とする
ものである。That is, the method for producing a granular paste according to the present invention involves spraying water onto fluidized water-soluble powder paste particles, drying them, and then drying them.
It is characterized by obtaining granules having the following properties.
(イ) 12メツシュ篩(JIS規格)を実質的に全治
が通過し、100メツシュ篩<JISM格)上に実質的
に令聞が残る粒面であること。(a) The grain surface must pass through a 12-mesh sieve (JIS standard) with substantially all grains and remain substantially clean on a 100-mesh sieve (JISM rating).
(0) 見掛は比容積が、糊料粉末原料の見掛は比容積
の少なくとも1.3倍であること。(0) The apparent specific volume of the paste powder raw material should be at least 1.3 times the specific volume.
効 果
本発明による粒状糊料は、前記したようにその単位粒状
物が水溶性粉末糊料の粒子間を水で結合したもの、であ
って前記の性質を有するものである。Effects As described above, the granular paste according to the present invention is a unit granule in which particles of a water-soluble powder paste are bonded by water, and has the properties described above.
従って、先願発明と同様に今までの水溶性粉末糊料が有
していた上記問題点を解決するとともに下記のような利
点をも有する。Therefore, like the prior invention, the above-mentioned problems of the conventional water-soluble powder pastes are solved, and the invention also has the following advantages.
(イ) ママコを形成せず、水に対して叩溶性がある。(b) It does not form a lump and is soluble in water.
従来の水溶性粒状糊料は、通常の撹拌により水に溶解す
る場合にママコを生じるのがふつうであリ、従来より、
このママコの形成防止ないし消失のため種々の方法が行
われてきたが、いずれの方法もその解決策とはならなか
った。しかしながら本発明の粒状糊料は、粒状糊料の粒
子間を水で結合させて粒状糊料としたものであるため、
ママコを形成せず、水に対する溶解性が著しく向上した
。Conventional water-soluble granular pastes usually produce lumps when dissolved in water by normal stirring;
Various methods have been used to prevent or eliminate the formation of mamako, but none of the methods has been a solution. However, since the granular paste of the present invention is made by bonding the particles of the granular paste with water,
No lumps were formed and the solubility in water was significantly improved.
(ロ) 粒状糊料本来の特性を実質的に変化さけない。(b) The original properties of the granular paste are not substantially changed.
ママコ形成を防止するにあたり、従来は粉末糊料をママ
コを生じにくい別の粒状糊料でコーティングするという
方法も行われていたが、このようにして得られた糊料は
、糊料本来の特性が失われ、さらには糊液粘度も著しく
変動するという不都合があった。In order to prevent mako formation, the conventional method was to coat the powdered glue with another granular paste that is less likely to cause mako, but the paste obtained in this way does not have the inherent properties of the glue. There were disadvantages in that the viscosity of the glue was lost and the viscosity of the glue also varied significantly.
これに対し、本発明の粒状糊料は、水を結合剤の代りと
して使用したものであるので(水溶性である原料粉末が
噴霧された水によっていくらか溶解したものが結合剤と
して機能している可能性がある)、製品粒状糊料は原料
粉末糊料本来の特性を実質的に損なうことなく保有して
いる。On the other hand, since the granular paste of the present invention uses water instead of a binder (the water-soluble raw material powder is somewhat dissolved by the sprayed water, it functions as a binder). ), the product granular paste retains the original properties of the raw powder paste without substantially impairing it.
従って、本発明による粒状糊料は、原料粉末糊料本来の
用途(たとえば安定剤)に使用することが可能であると
いえる。Therefore, it can be said that the granular paste according to the present invention can be used for the original purpose of the raw powder paste (for example, as a stabilizer).
(ハ) 取扱いが簡単である。(c) Easy to handle.
従来の水溶性粉末糊料は、飛散性、流動性、および充填
性に問題があり、また保存中に固結を起こず等、好まし
くない物性を有していた。Conventional water-soluble powder pastes have problems with scattering properties, fluidity, and filling properties, and also have unfavorable physical properties such as not caking during storage.
しかしながら、水溶性粉末糊料を粒状化してなる本発明
の粒状糊料は飛散性および付着性が改善され、凝集性が
ないので保存性にもすぐれており、また流動性が良好で
あるところから適当な容a法で計ることもできるので取
扱いが簡単である。However, the granular paste of the present invention, which is obtained by granulating a water-soluble powder paste, has improved scattering and adhesion properties, has no agglomeration, and has excellent storage stability, and also has good fluidity. It is easy to handle because it can be measured using an appropriate volume a method.
11血豆入h1」
粒□状糊料
本発明の粒状糊料は、「水溶性粉末糊料に水を噴霧する
ことによって造粒された粒子からなるもの」である。こ
の場合の「水溶性粉末糊料」とは、分散系の安定化、ゲ
ル化、増粘、皮膜形成、テクスチャーの向上等の目的の
ためにあるいは結合剤として使用され得るもの、である
。このような水溶性粉末糊料としては、例えば、ペクチ
ン、キリンタンガム、ローカストピーンガム、グアーガ
ム、アラビアゴム、アルギン酸ナトリウム等の天然品や
、ヒトOキシプOビルセルロース、メチルセルロース、
カルボキシメチルセル
ナトリウム等のセルロース誘聯体およびポリビニルビO
リドン、ポリアクリル酸ナトリウム等の化学合成品があ
る。本発明の粒状糊料の原料として用いられる粉末糊料
は、上記の単一成分からなってもあるいは二つ以上の任
意の組合せからなってもよく、またこれらに他の成分を
適宜配合したもの(例えば動物性蛋白質改良剤として「
エクスホーマ」 (日本コロイド株式会社)等がある)
からなっていてもよい。11 Blood bean h1'' Granular square paste The granular paste of the present invention is "consisting of particles granulated by spraying water on a water-soluble powder paste." The "water-soluble powder paste" in this case is one that can be used for purposes such as stabilizing, gelling, thickening, film formation, and improving texture of a dispersion system, or as a binder. Such water-soluble powder pastes include, for example, natural products such as pectin, giraffe gum, locust pea gum, guar gum, gum arabic, sodium alginate, human O-oxypyl cellulose, methyl cellulose,
Cellulose derivatives such as carboxymethyl cell sodium and polyvinyl vinyl
There are chemically synthesized products such as lydone and sodium polyacrylate. The powdered paste used as a raw material for the granular paste of the present invention may be composed of the above-mentioned single component or any combination of two or more, or may be a mixture of these and other components as appropriate. (For example, as an animal protein improver,
(Nippon Colloid Co., Ltd.) etc.)
It may consist of.
「水を噴霧する」というときの水の種類、水滴の大きさ
および水の5その他は、原料粉末糊料の粒子が凝集して
所定の粒状特性(詳細後記)を得るような任意のもので
ありうる。水は必要に応じてアルコールその他の水溶性
有礪溶剤、好ましくは易揮発性のもの)あるいは製品粉
末糊料中に成分として無機塩その他を含有させたいとき
にはその成分を溶解させたものであってもよいが(その
場合にも、結合剤を使用しないという本発明の精神から
いって、これらの物質が溶存している水は粘度が水自身
のそれと大差のないものでなければならない)、本発明
の一般的ないし代表的な態様は通常の水、すなわち、上
水道水、蒸留水、精製水、その他、を使用することであ
る(水滴の山およびその量については後記)。When "spraying water", the type of water, the size of the water droplets, and other parameters may be arbitrary such that the particles of the raw powder paste aggregate to obtain the desired granular characteristics (details will be described later). It's possible. The water may be an alcohol or other water-soluble solvent (preferably an easily volatile solvent, if necessary) or, if necessary, an inorganic salt or other component dissolved therein in the powdered paste product. (Even in that case, in keeping with the spirit of the present invention of not using a binder, the water in which these substances are dissolved must have a viscosity that is not much different from that of the water itself.) A general or typical embodiment of the invention is to use regular water, ie, tap water, distilled water, purified water, etc. (more on drop piles and amounts below).
本発明による粉状糊料は、12メツシュ篩を実質的に全
aが通道し、100メツシュ篩上に実質的に全量が残る
という程度の粒度のものである(r5jのメツシュはJ
IS規格によるものである)。The powdery paste according to the present invention has a particle size such that substantially all of it passes through a 12-mesh sieve and substantially all of it remains on a 100-mesh sieve (r5j mesh is J
(according to IS standards).
また°、見掛は比容積が、糊料粉末原料の比容積の少な
くとも1.3倍程度であり、好ましくは1、5倍程度以
上のもの、である。ここで見掛り比容積とは、最疎(ゆ
るみ)見掛は比容積のことをいい、通常用いられる見掛
は比重の逆数、すなわち、単位質量の粒子が充填されて
占める容積をいい、cc/ 9の単位で表されるものを
いう。そして、これは、本発明では、粒子の多孔性を調
べる一つの手段である。なお、比容積の測定はJISK
5101の方法によるものとし、具体的には、適当な機
器、たとえばパウダーデスタ−(ホソカワミクロン■〕
で行うことができる。本発明の糊料は、この見掛は比容
積が1.3倍以上となっている。このことは、糊料粉末
原料と比べて本発明の糊料は、粒子間空隙が増加したこ
とが示唆され、また多孔質構造となっていることも示唆
される。Further, the apparent specific volume is at least about 1.3 times, preferably about 1.5 times or more, the specific volume of the paste powder raw material. Here, the apparent specific volume refers to the sparsest (looseness) apparent specific volume, and the commonly used apparent volume refers to the reciprocal of specific gravity, that is, the volume occupied by particles of unit mass filled, cc / Refers to something expressed in units of 9. This, in turn, is one means of examining particle porosity in the present invention. In addition, the measurement of specific volume is based on JISK.
5101 method, and specifically, using a suitable device, such as a powder dester (Hosokawa Micron ■).
It can be done with The paste of the present invention has a specific volume that is 1.3 times or more greater than this apparent volume. This suggests that, compared to the paste powder raw material, the paste of the present invention has increased interparticle voids, and also suggests that it has a porous structure.
従って、粒子内部での水の浸透が早くなる(溶解性の向
上)とともにママコの発生をも防止することができる(
後記参考例参照)。Therefore, water permeates inside the particles faster (improves solubility), and also prevents the formation of lumps (
(See reference example below).
粒状糊料の¥J造
本発明の粒状糊料は「流動化された水溶性粉末糊料に水
を噴霧したのち乾燥して粒状物を得る」といつ先願発明
に開示された方法と同様の方法に従って製造することが
できる。¥J construction of granular paste The granular paste of the present invention is similar to the method disclosed in the earlier invention, in which ``water is sprayed onto a fluidized water-soluble powder paste and then dried to obtain granules.'' It can be manufactured according to the method of
このような方法は、原料の粉末を気流によってi初層と
し、これに液体を噴霧して造粒することからなる方法に
従って行うことができ、流動層造粒装置によって行うの
がふつうである。Such a method can be carried out by making the raw material powder into an initial layer using an air current, and then granulating it by spraying a liquid thereon, and is usually carried out using a fluidized bed granulator.
その一実施態様を述べれば下記の通りである。One embodiment thereof is as follows.
まず、水溶性粉末糊料を流動層造粒装置にいれたのち(
この際に必要に応じた分散剤を投入してもよい)、これ
に50℃〜100℃で加温した温風を下方より通じて粉
末糊料を流動化させる。ついで、ここで形成された粉末
糊料の流動層に水(好ましくは精製水)を噴霧したのち
、乾燥を行うことにより、粒状1[を得ることができる
。First, after putting the water-soluble powder paste into a fluidized bed granulator (
At this time, a dispersant may be added as required), and hot air heated at 50° C. to 100° C. is passed from below to fluidize the powder paste. Next, after spraying water (preferably purified water) onto the fluidized bed of the powdered paste formed here, granules 1 can be obtained by drying.
また、他の実施態様としては、水溶性粉末糊料を流動層
造粒装置にいれたのち、下方より冷風を通じて粉末糊料
の流動化を行い、これに水を噴霧したのち冷風を熱風に
切り換える方法によっても本発明の粒状糊料を得ること
ができる。In another embodiment, a water-soluble powder paste is put into a fluidized bed granulator, the powder paste is fluidized by blowing cold air from below, water is sprayed thereon, and then the cold air is switched to hot air. The granular paste of the present invention can also be obtained by this method.
ここで用いられる水溶性粉末糊料および水は上記した通
りであるが、水の使用量および噴霧条件は下記の通りで
ある。水の使用量は、原料である水溶性粉末糊料の種類
、目的として得る粒状糊料の粒径等に合せて適宜換える
のが好ましいが、本発明においては糊料原料に対し5〜
50%(W/W〉が好ましい。噴霧条件は、本発明の実
施例で用いたユニブラット流動層造粒機(小型造粒装置
)の場合は噴霧速度10〜50al!/分、噴霧圧力0
.5〜2にg/Cm2で行うのがふつうである。なお、
このような噴霧速度および噴霧圧は流動層、造粒装置に
より調整可能であり、また装置の大小、造粒物の大きさ
等にあわせて適宜選定すべきであることはいうまでもな
い。The water-soluble powder paste and water used here are as described above, but the amount of water used and the spraying conditions are as follows. The amount of water used is preferably changed depending on the type of water-soluble powder paste used as a raw material and the particle size of the granular paste to be obtained.
50% (W/W>) is preferable. In the case of the Uniblat fluidized bed granulator (small granulator) used in the examples of the present invention, the spraying conditions are a spraying rate of 10 to 50al!/min, and a spraying pressure of 0.
.. It is usually carried out at 5 to 2 g/Cm2. In addition,
It goes without saying that such spray speed and spray pressure can be adjusted using a fluidized bed or a granulating device, and should be appropriately selected depending on the size of the device, the size of the granulated material, etc.
このようにして本発明の粒状糊料製造法に従えば、流動
化された粉末糊料に水が噴霧されることにより粉末m料
の粒子が結合し、さらにこれに温風を通じることにより
多孔質構造を有する凝集物が形成され(−次凝集物)、
そしてさらに−次凝集物が結合してより大きな凝集物に
なる、というように粉末糊料結合物形成→凝集物形成と
いう過程がくり返えされることによって、本発明の粒状
糊料が得られると推定される。In this way, according to the method for producing granular paste of the present invention, water is sprayed on the fluidized powder paste to bond the particles of the powder paste, and then hot air is passed through this to form porous adhesives. Aggregates with a qualitative structure are formed (-order aggregates),
Then, the granular paste of the present invention can be obtained by repeating the process of forming a powder paste binder and forming an aggregate, in which the next aggregate is combined to form a larger aggregate. Presumed.
このようにして得られる本発明粒状糊料は、l!!!想
的には、各粒子が一次粒子ないし二次粒子(二次以降の
ものを包含する)の表面での接着により形成された多孔
質構造を持つものであると解される。従って、本発明に
よる粒状糊料はママコを形成しな(なるのであるが、こ
れは、原料である粉末糊料と比較して、本発明による糊
料の方が単位重量当りの表面積が小さくなるからである
。また、本発明による粒状糊料は、各々の粒子が多孔質
構造となっている。従って、粒子内部への水の浸透が非
常に早くなっている(すなわち、溶解性が向上している
)。The granular paste of the present invention thus obtained is l! ! ! It is conceptually understood that each particle has a porous structure formed by adhesion on the surface of a primary particle or a secondary particle (including secondary particles). Therefore, the granular paste according to the present invention does not form lumps, but this is because the paste according to the present invention has a smaller surface area per unit weight than the powdered paste that is the raw material. In addition, in the granular paste according to the present invention, each particle has a porous structure.Therefore, water permeates into the inside of the particles very quickly (that is, the solubility is improved). ing).
激−コL−μ
実施例1
ユニブラット(UNIGLATT)流動層造粒II(四
人川原製作所)を用い、キザンタンガム500g(80
メツシュ全通、大日本製薬■)を温風(90℃)で流動
化させたのち、これに精製水150gを噴霧速度30m
/分、噴霧圧1.25に9/C12の条件下で噴霧し、
ついで乾燥することにより、粒状糊料を造粒した。Example 1 Using UNIGLATT fluidized bed granulation II (Yonin Kawara Seisakusho), 500 g of xanthan gum (80
Metshu Zentsu, Dainippon Pharmaceutical ■) was fluidized with warm air (90°C), and then 150 g of purified water was sprayed at a speed of 30 m.
/min, spraying pressure 1.25 under the conditions of 9/C12,
The granular paste was then granulated by drying.
実施例2
実施例1と同じ装置を用い、ヒトOキシブOビルセルロ
ース(Lタイプ、以下HPC−Lという)500!7
(100メツシュバス77%、日本四速@J)を温風(
90℃)で流動化させたのら、これに精製水80gを噴
霧速度20d/分、噴霧圧1 、25N!?/cm2の
条件下で噴霧し、ついで乾燥することにより、粒状糊料
を造粒した。Example 2 Using the same equipment as in Example 1, human Oxib O-bil cellulose (L type, hereinafter referred to as HPC-L) 500!7
(100 mesh bus 77%, Japan 4 speed @J) with warm air (
After fluidizing it at 90°C, 80g of purified water was sprayed at a rate of 20d/min and a spraying pressure of 1.25N! ? The granular paste was granulated by spraying under the condition of /cm2 and then drying.
実施例3
実施例1および2と同一の装置を用い、カルボキシメヂ
ルビル印−ス・ナトリウム(以下CMC−Naという)
4009(100メツシュ全通、第一工業製薬味)を温
風(90℃)で流動化させたのち、これに精製水100
gを噴霧速[a300Id/分、噴霧圧1.25に9/
Cg12の条件下で噴霧し、ついで乾燥することにより
、粒状糊料を造粒した。Example 3 Using the same equipment as in Examples 1 and 2, carboxymedylvinyl chloride sodium (hereinafter referred to as CMC-Na) was prepared.
4009 (all 100 mesh, Daiichi Kogyo Seiyaku flavor) was fluidized with warm air (90°C), and then 100% purified water was added to it.
g to spray rate [a300Id/min, spray pressure 1.25 to 9/
A granular paste was granulated by spraying under Cg12 conditions and then drying.
参考例1
下記の溶解法に従って、従来の粉末糊料と本発明の粒状
糊料との溶解時間を測定した。Reference Example 1 According to the following dissolution method, the dissolution time of a conventional powder paste and a granular paste of the present invention was measured.
700ccステンレス鋼製ビーカーに精製水200cc
を入れ、一定の速度(約500rDIl)で攪拌(撹拌
羽根4枚)を行いながら、試料を投入した。そして試料
が完全に分散、溶解して粘稠な水溶液になるまでの時間
を測定した。200cc of purified water in a 700cc stainless steel beaker
was added, and the sample was added while stirring (four stirring blades) at a constant speed (approximately 500 rDIl). Then, the time required for the sample to be completely dispersed and dissolved to become a viscous aqueous solution was measured.
そのときの結果を第1表に示す。The results are shown in Table 1.
本 粒状糊料はすべて100メツシュの篩で篩分した篩
上の粒状糊料を使用した。All of the granular pastes were sieved through a 100-mesh sieve.
*傘 溶解時間は3回測定したときの平均値である。*Umbrella Dissolution time is the average value of three measurements.
この結果より、本発明の糊料は、従来の糊料と比較して
、その溶解性が著しく向上しているといえる。From this result, it can be said that the paste of the present invention has significantly improved solubility compared to conventional pastes.
参考例2
実施例1.2および3で得られた本発明の糊料を12メ
ツシュ<1oooμ)および100メツシュ(149μ
)で篩分けした時の粒度を調べた。Reference Example 2 The paste of the present invention obtained in Examples 1.2 and 3 was applied to 12 mesh<1oooμ) and 100 mesh (149μ).
) The particle size when sieved was examined.
そして、その糊料の粒1度の分布状況を調べた。そのと
きの結果を第2表に示す。Then, the distribution of particles of the glue was investigated. The results are shown in Table 2.
なお、12メツシュ残留物は1.01+111φスクリ
ーンを用い、パワーミルによる破砕処理で、12メツシ
ュ篩通過、100メツシュ篩上残留物を得ることができ
る。The 12-mesh residue can be crushed using a power mill using a 1.01+111φ screen to obtain a residue that passes through the 12-mesh sieve and remains on the 100-mesh sieve.
参考例3
本発明の11料とその原料粉末との物性の比較を行った
。物性としでは、累積粒度および見掛り比容@a(cc
/g)を調べた。篩上の見11)1ノ比容積は、パウダ
ーテスター〔ホソカワミクOン曲〕で測定した。また、
累積粒度は、上記パウダーデスタ−を使用し、レオスタ
ット4目盛で3分間振動を行うことによって測定した。Reference Example 3 The physical properties of Material 11 of the present invention and its raw material powder were compared. As for physical properties, cumulative particle size and apparent specific volume @a (cc
/g) was investigated. 11) The specific volume of the sieve was measured using a powder tester (Hosokawamiku O-Ken). Also,
The cumulative particle size was measured using the above-mentioned Powder Destar by vibrating for 3 minutes at 4 rheostat scales.
そのときの結果を13表に示す。The results are shown in Table 13.
この結果より、本発明の糊料の見掛は比容積は、いずれ
も原料の1.5倍以上になっており、本発明の糊料は多
孔質構造を有していることが示唆される。従って、参考
例1で示したように溶解性が著しく向上している。From these results, the apparent specific volume of the paste of the present invention is 1.5 times or more that of the raw material, suggesting that the paste of the present invention has a porous structure. . Therefore, as shown in Reference Example 1, the solubility is significantly improved.
Claims (1)
た粒子からなるものであって、下記の性質を有すること
を特徴とする粒状糊料。 (イ)12メッシュ篩(JIS規格)を実質的に全量が
通過し、100メッシュ篩(JIS規格)上に実質的に
全量が残る粒度であること。 (ロ)見掛け比容積が、糊料粉末原料の見掛け比容積の
少なくとも1.3倍であること。 2、流動化された水溶性粉末糊料粒子に水を噴霧したの
ち乾燥して、下記の性質を有する粒状物を得ることを特
徴とする粒状糊料の製造法。 (イ)12メッシュ篩(JIS規格)を実質的に全量が
通過し、100メッシュ篩(JIS規格)上に実質的に
全量が残る粒度であること。 (ロ)見掛け比容積が、糊料粉末原料の見掛け比容積の
少なくとも1.3倍であること。[Scope of Claims] 1. A granular paste comprising particles granulated by spraying water on a water-soluble powder paste, characterized by having the following properties: (a) The particle size is such that substantially the entire amount passes through a 12 mesh sieve (JIS standard) and substantially the entire amount remains on a 100 mesh sieve (JIS standard). (b) The apparent specific volume is at least 1.3 times the apparent specific volume of the paste powder raw material. 2. A method for producing a granular paste, which comprises spraying water on fluidized water-soluble powder paste particles and then drying them to obtain granules having the following properties. (a) The particle size is such that substantially the entire amount passes through a 12 mesh sieve (JIS standard) and substantially the entire amount remains on a 100 mesh sieve (JIS standard). (b) The apparent specific volume is at least 1.3 times the apparent specific volume of the paste powder raw material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61168956A JPS6324865A (en) | 1986-07-17 | 1986-07-17 | Granular paste and production thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61168956A JPS6324865A (en) | 1986-07-17 | 1986-07-17 | Granular paste and production thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6324865A true JPS6324865A (en) | 1988-02-02 |
JPH0575369B2 JPH0575369B2 (en) | 1993-10-20 |
Family
ID=15877670
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61168956A Granted JPS6324865A (en) | 1986-07-17 | 1986-07-17 | Granular paste and production thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6324865A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0964024A1 (en) * | 1998-06-11 | 1999-12-15 | Fuji Oil Company, Ltd. | Process for producing granulated water-soluble polysaccharide |
WO2001032132A3 (en) * | 1999-11-03 | 2002-01-03 | Hercules Inc | Process for making toothpaste using agglomerated dispersible polymers |
JP2007006745A (en) * | 2005-06-29 | 2007-01-18 | Taiyo Kagaku Co Ltd | Viscosity regulator |
JP2008161092A (en) * | 2006-12-27 | 2008-07-17 | Sanei Gen Ffi Inc | Method for granulating powder |
JP2009525391A (en) * | 2006-01-30 | 2009-07-09 | ハーキュリーズ・インコーポレーテッド | Method for producing cellulose ether dispersible in cold water and use thereof |
JP2010081943A (en) * | 2005-03-11 | 2010-04-15 | Taiyo Kagaku Co Ltd | Thickening composition improved in viscosity development |
WO2021010257A1 (en) * | 2019-07-12 | 2021-01-21 | 森永乳業株式会社 | Composition for imparting thickness |
-
1986
- 1986-07-17 JP JP61168956A patent/JPS6324865A/en active Granted
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0964024A1 (en) * | 1998-06-11 | 1999-12-15 | Fuji Oil Company, Ltd. | Process for producing granulated water-soluble polysaccharide |
WO2001032132A3 (en) * | 1999-11-03 | 2002-01-03 | Hercules Inc | Process for making toothpaste using agglomerated dispersible polymers |
JP2010081943A (en) * | 2005-03-11 | 2010-04-15 | Taiyo Kagaku Co Ltd | Thickening composition improved in viscosity development |
US7744942B2 (en) | 2005-03-11 | 2010-06-29 | Taiyo Kagaku Co., Ltd. | Thickening composition having improved viscosity-emerging property |
JP2007006745A (en) * | 2005-06-29 | 2007-01-18 | Taiyo Kagaku Co Ltd | Viscosity regulator |
JP2009525391A (en) * | 2006-01-30 | 2009-07-09 | ハーキュリーズ・インコーポレーテッド | Method for producing cellulose ether dispersible in cold water and use thereof |
JP2008161092A (en) * | 2006-12-27 | 2008-07-17 | Sanei Gen Ffi Inc | Method for granulating powder |
WO2021010257A1 (en) * | 2019-07-12 | 2021-01-21 | 森永乳業株式会社 | Composition for imparting thickness |
JPWO2021010257A1 (en) * | 2019-07-12 | 2021-10-21 | 森永乳業株式会社 | Composition for thickening |
Also Published As
Publication number | Publication date |
---|---|
JPH0575369B2 (en) | 1993-10-20 |
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