JPH01293128A - Granulating method - Google Patents

Granulating method

Info

Publication number
JPH01293128A
JPH01293128A JP12290588A JP12290588A JPH01293128A JP H01293128 A JPH01293128 A JP H01293128A JP 12290588 A JP12290588 A JP 12290588A JP 12290588 A JP12290588 A JP 12290588A JP H01293128 A JPH01293128 A JP H01293128A
Authority
JP
Japan
Prior art keywords
freeze
soln
liquid
granulated
nonhydrated
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.)
Pending
Application number
JP12290588A
Other languages
Japanese (ja)
Inventor
Akiji Kotani
明司 小谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Amano Jitsugyo Co Ltd
Original Assignee
Amano Jitsugyo Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Amano Jitsugyo Co Ltd filed Critical Amano Jitsugyo Co Ltd
Priority to JP12290588A priority Critical patent/JPH01293128A/en
Publication of JPH01293128A publication Critical patent/JPH01293128A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently produce granular substance having a constant shape and rapidly soluble without using a mold by dropping an aq. soln. incorporating useful components into nonhydrated liquid held at low temp. and freeze- granulating these components and thereafter freeze-drying them under vacuum. CONSTITUTION:In the formulation field of remedy and agricultural chemicals, etc., an aq. soln. is prepared by adding a shaping agent such as a surfactant or a binding agent such as starch in accordance with necessity to the available components such as extracts and coloring matters. This aq. soln. is dropt into nonhydrated liquid such as kerosene which has been held at low temp. sufficient to freeze-solidify the aq. soln. and the available components are freeze- granulated. Thereafter the freeze-granulated substance is separated from the nonhydrated liquid and freeze-dried under vacuum. When performing granulation by such a way, the shape and particle diameter of the granulated substance are made uniform and the change of particle diameter is made easy. Furthermore a mold is not used and the granulated substance is rapidly solubilized in water and the available components are not thermally denaturated.

Description

【発明の詳細な説明】 イ8発明の利用分野 本発明は、医薬、農薬、各種の化成品の製剤分野、なら
びに食品の製剤分野において利用しうる。
DETAILED DESCRIPTION OF THE INVENTION A.8 Field of Application of the Invention The present invention can be utilized in the field of pharmaceutical, agrochemical, and various chemical product formulations, as well as the food formulation field.

口、従来の技術 従来、有用成分を含む製剤の粒状物の造粒方法にはいく
つかのものが知られている。
BACKGROUND OF THE INVENTION Conventionally, several methods are known for granulating granules of pharmaceutical preparations containing useful ingredients.

■湿式不定形造粒乾燥法 有用成分と賦形剤もしくは結着剤の粉状混合物に水等の
溶媒を散布しつつ1通風しながら乾燥し。
■Wet amorphous granulation drying method A powder mixture of useful ingredients and excipients or binders is sprayed with a solvent such as water and dried with ventilation.

湿潤状態で凝集した小塊を転勤状態下で造粒する方法で
ある。
This is a method in which small agglomerated agglomerates in a wet state are granulated under transfer conditions.

この場合には生成粒子の形状は不定形であるとともに、
かなり広い粒度分布を有する。
In this case, the shape of the generated particles is amorphous, and
It has a fairly wide particle size distribution.

(5)噴霧乾燥造粒法 有用成分と賦形剤もしくは結着剤を含む水溶液を熱風中
に噴霧して乾燥造粒する方法である。
(5) Spray-drying granulation method This is a method in which an aqueous solution containing useful ingredients and excipients or binders is sprayed into hot air and dried and granulated.

生成する粒子は0.2羽以下の微粒子であり、広範囲の
粒度分布を有する。
The particles produced are fine particles of 0.2 feathers or less and have a wide range of particle size distribution.

0凍結解砕−真空凍結乾燥法 有用成分と賦形剤もしくは結着剤を含む塊状の凍結物を
解砕し、所望の大きさの粒状物を分級して収集し、真空
凍結乾燥する方法である。
0 Freeze-Thaw - Vacuum Freeze-Drying A method in which frozen blocks containing useful ingredients and excipients or binders are thawed, granules of desired size are classified and collected, and then vacuum freeze-dried. be.

生成する粒子は不定形である。The particles produced are amorphous.

(IIP(C)の変法であり、型中に原液を型中に流し
こみ。
(This is a modified method of IIP (C), in which the stock solution is poured into a mold.

凍結成形してから真空凍結乾燥する方法である。This method involves freeze-molding and then vacuum freeze-drying.

生成する粒子は定形であるが2多数の型を用意する必要
があり、型の製作、清掃等にコストが多くかかり、能率
的な方法とは言い難い。また1球状物を得ることは困難
である。
Although the particles produced are of regular shape, it is necessary to prepare two molds, and the manufacturing and cleaning of the molds is costly, so it cannot be said to be an efficient method. Moreover, it is difficult to obtain a single spherical object.

■押し出し造粒法 有用成分、賦形材もしくは結着剤を含む高粘度の溶液、
もしくは線状物を細いノズルより押し出し、一定長さに
切断して通風乾燥して成形する方法である。
■Extrusion granulation method A high viscosity solution containing useful ingredients, excipients or binders,
Alternatively, a linear material is extruded through a thin nozzle, cut to a certain length, and dried through ventilation to form the material.

生成する粒子はベレット状であり、生成する粒子は即溶
性に乏しい。
The particles produced are pellet-shaped and have poor immediate solubility.

[F]打錠法 有用成分、賦形剤もしくは結着剤の混合粉体を型中に入
れて高圧にて打錠成形するものである。
[F] Tableting method A mixed powder of useful ingredients, excipients, or binders is placed in a mold and compressed into tablets under high pressure.

本性では型が多数必要であること、生成する粒状物は高
密度で即溶性に乏しい等の難点がある。
In nature, there are drawbacks such as the need for a large number of molds, and the granules produced are highly dense and have poor immediate solubility.

%i′発明の解決すべき課題 本発明の目的は、型を用いることなく、能率的に、一定
の形状を有し、かつ、高い即溶性を有する粒状物を製造
する方法を提供せんとするものである。
%i' Problems to be Solved by the Invention An object of the present invention is to provide a method for efficiently producing granules having a constant shape and high immediate solubility without using a mold. It is something.

今日2造粒による製剤化は医薬、農薬、各種化成品2食
品の分野において。
Today, formulations using granulation are used in the fields of pharmaceuticals, agrochemicals, and various chemical products.

■取り扱い性(計量、吸湿防止、流動性、包装性溶解時
のまま粉発生防止等)の向上。
■Improved handling (measurement, prevention of moisture absorption, fluidity, packaging ability, prevention of powder generation during dissolution, etc.).

の)外観の向上。) Improved appearance.

(q使用時の溶解性の調整。(Adjustment of solubility when using q.

等を目的として広く利用されている。It is widely used for such purposes.

本発明者は球状、もしくはそれに近似する一定の粒度(
形状と粒径)の分布のそろった゛、即溶性を有する粒状
物を能率よく製造する方法を探索。
The present inventor has determined that the particle size is spherical or has a certain particle size (approximately spherical).
We are exploring ways to efficiently produce granular materials with a uniform distribution (shape and particle size) and immediate solubility.

検討し本発明に到達した。After much research, we arrived at the present invention.

二1発明の構成 本発明は以下の工程を結合して構成されるものである。21 Composition of the invention The present invention is constructed by combining the following steps.

■有用成分と、必要ならば賦形剤あるいは結着剤を含む
水溶液を、その水溶液が凍結固化するに充分な低温に保
持されt:非水和性の液体l1llliこ滴化し。
(2) An aqueous solution containing the useful ingredients and, if necessary, an excipient or binder, is kept at a low enough temperature to freeze and solidify the aqueous solution, and the aqueous solution is reduced to a non-hydratable liquid.

凍結造粒する工程。Freeze granulation process.

■かくして得られた凍結造粒物を非水和性の液体より分
別する工程。
■The step of separating the thus obtained frozen granules from non-hydratable liquids.

(C)分別された凍結造粒物を真空凍結乾燥する工程。(C) A step of vacuum freeze-drying the separated frozen granules.

以下に、(8)、@、(C)の各工程を詳説したい。Below, I would like to explain each step (8), @, and (C) in detail.

■滴下・凍結造粒工程 有用成分としては2例えば医薬(合成品、天然抽出品)
、農薬、各種の化成品2種々のエキス類。
■Dripping/freezing granulation process Useful ingredients include 2, such as pharmaceuticals (synthetic products, natural extracts)
, pesticides, various chemical products, 2 various extracts.

色素類、飲料(コーヒー、茶類(日本茶(緑茶。Colors, beverages (coffee, teas (Japanese tea (green tea).

番茶、麦茶、はうじ茶等)、紅茶、プアール茶。(bancha, barley tea, haujicha, etc.), black tea, puerh tea.

ココア、ジュース類2清涼飲料類等)等の種々のものを
あげうる。
Cocoa, juices, soft drinks, etc.).

有用成分としては人体への摂取を目的とするもののみな
らず、屋内、屋外への散布、化成品製品の使用時に添加
等を目的として使用されるものをも含む。
Useful ingredients include not only those intended for ingestion into the human body, but also those used for purposes such as spraying indoors and outdoors, and adding when using chemical products.

有用成分は必ずしも水に溶解するものである必要はなく
、不溶性のものでも懸濁、ないしは乳化の状態で本発明
に供することができる。
The useful components do not necessarily have to be soluble in water, and even insoluble components can be used in the present invention in a suspended or emulsified state.

有用成分を水溶液(場合により懸濁、あるいは乳化)と
する際に、溶解助剤(例えば界面性剤。
A solubilizing agent (for example, a surfactant) is used when useful ingredients are made into an aqueous solution (suspended or emulsified as the case may be).

酸、アルカリ、キレート剤、塩類、PH調整剤等)。acids, alkalis, chelating agents, salts, PH adjusters, etc.).

香料2色部、賦形剤(例えば鉱物粉末(ベントナイト、
ケイソウ上、カオリン、タルク、ゼオライト、シリカゲ
ル等)2合成樹脂床(ポリスチレン。
Fragrance two colors, excipients (e.g. mineral powders (bentonite,
2 synthetic resin beds (polystyrene, kaolin, talc, zeolite, silica gel, etc.)

ポリエチレン、ポリプロピレン、ベークライト等)天然
高分子(キトサン、キチン、でん粉、ゼラチン、セルロ
ーズ、パルプ、多糖類(アラビアガム。
polyethylene, polypropylene, Bakelite, etc.) natural polymers (chitosan, chitin, starch, gelatin, cellulose, pulp, polysaccharides (gum arabic).

キサンタンガム、グアガム、タラガム、寒天、アルギネ
ート、トラガントガム、フルセラン、カラギナン、ロー
カストビーンガム、タマリンドガム等)))、 結着剤
(ポリビニアルコールとその誘導体。
xanthan gum, guar gum, tara gum, agar, alginate, tragacanth gum, furceran, carrageenan, locust bean gum, tamarind gum, etc.)), binders (polyvinyl alcohol and its derivatives).

セルロースのカルボキシアルキルエーテル類、各種のガ
ム類、カゼインナトリウム等、糖類(乳糖2デキストリ
ン、可溶性でんぷん、水あめ、グルコース等))等を添
加することができる。
Carboxyalkyl ethers of cellulose, various gums, sodium caseinate, sugars (lactose 2-dextrin, soluble starch, starch syrup, glucose, etc.), etc. can be added.

有用成分単体でも真空凍結乾燥後の粒状物の保形性を維
持しうる場合もあるが(例えば後の実施例4に示したカ
ラメル)、多くの場合粒状構造を使用時までの取扱いに
おいて維持するためには賦形剤もしくは結着剤の添加が
必要なことが多い。
Although there are cases where the useful ingredient alone can maintain the shape retention of granules after vacuum freeze-drying (for example, the caramel shown in Example 4 below), in many cases the granular structure is maintained during handling until use. This often requires the addition of excipients or binders.

粒状物の溶解性を調整するために油脂類(各種の動植物
油類、レシチン類、グリセリン七)、あるいはジエステ
ル類、ワックス類、トール油、硫酸化油類等)2発泡剤
(炭酸塩類9重炭酸塩類等)。
To adjust the solubility of granules, oils (various animal and vegetable oils, lecithin, glycerin), diesters, waxes, tall oil, sulfated oils, etc.), blowing agents (carbonates, etc.) carbonates, etc.).

結晶性セルロースの微粉等を添加してもよい。Fine powder of crystalline cellulose or the like may be added.

水溶液を調製するにあたっては適宜、加熱、かる場合に
は適宜に加温して用いることもできる。
When preparing an aqueous solution, it can be heated as appropriate, and in some cases, it can be heated appropriately before use.

非水和性の液体としては1例えば炭化水素類(灯油、軽
油、揮発油、n−ヘキサン、ペンタン、ブタン、液化石
油ガス、トルエン等)、ハロ炭化水素類(クロロホルム
、ブロモホルム、ジクロルメタン、ジクロルエタン、パ
ークロルエチレン、フロン類等)、エーテル類、エステ
ル類、ケトン類。
Examples of non-hydratable liquids include hydrocarbons (kerosene, light oil, volatile oil, n-hexane, pentane, butane, liquefied petroleum gas, toluene, etc.), halohydrocarbons (chloroform, bromoform, dichloromethane, dichloroethane, perchloroethylene, fluorocarbons, etc.), ethers, esters, ketones.

油脂類(動植物油2合成トリグリセリド類)、液化ガス
類(液化チッ素、液化エタン、液体空気。
Oils and fats (animal and vegetable oils, 2 synthetic triglycerides), liquefied gases (liquefied nitrogen, liquefied ethane, liquid air).

液体炭酸ガス等)等の単一、あるいは任意の混合溶媒を
用いればよい。
A single solvent such as liquid carbon dioxide gas, etc., or any mixed solvent may be used.

非水相性の液体は滴下する水溶液の固化温度よりも低く
保持し、所望によってはゆるくがくはんしておく。
The non-aqueous liquid is maintained at a temperature lower than the solidification temperature of the aqueous solution to be added dropwise, and is slightly stirred if desired.

滴下された水溶液は表面張力によって球状に近い形状に
成形されるが、非水和性の溶媒の温度が極端に低い場合
には成形の行なわれる前に凍結固化するので、液体の深
さに応じて温度匂配を持たせ、上層はやや高い温度にし
ておくこともできる。
The dropped aqueous solution is formed into a nearly spherical shape due to surface tension, but if the temperature of the non-hydratable solvent is extremely low, it freezes and solidifies before forming. It is also possible to create a temperature gradient by keeping the upper layer at a slightly higher temperature.

滴下はノズルより吐出することにより行なわれ。Dripping is performed by discharging from a nozzle.

ノズルの口径、形状、水溶液の粘度を変えることにより
粒状物の粒径を変えることができる。
The particle size of the granular material can be changed by changing the diameter and shape of the nozzle and the viscosity of the aqueous solution.

■凍結粒状物と非水和性の液体との分別工程口過、ある
いは非水相性の液体を蒸発させることにより容易に両者
を分別しうろ。非水和性の液体が高沸点の場合には1口
過後、凍結粒状物を低沸点の溶媒にて洗えばよい。
■Separation process of frozen granules and non-hydratable liquid The two can be easily separated by filtration or by evaporating the non-aqueous liquid. If the non-hydratable liquid has a high boiling point, the frozen granules may be washed with a low boiling point solvent after one sip.

0真空凍結乾燥工程 凍結粒状物を常法に従って回分式、あるいは連続式の真
空凍結乾燥に付する。すなわち、 1Torr以下、好
ましくは0.5 Torr以下の高真空下に数時間〜数
十時間程度、適宜たな加熱を行ないつつ。
0 Vacuum freeze-drying process The frozen granules are subjected to batch or continuous vacuum freeze-drying according to a conventional method. That is, while performing appropriate heating under a high vacuum of 1 Torr or less, preferably 0.5 Torr or less, for several hours to several tens of hours.

水分率5%以下程度にまで乾燥する。Dry to a moisture content of 5% or less.

以上のような工程に従って本発明は実施されるが2所望
により、得られる粒状物に着色、コーティング、抗酸化
処理等をさらに施してもよい。
The present invention is carried out according to the steps described above, but if desired, the resulting granules may be further subjected to coloring, coating, anti-oxidation treatment, etc.

ホ1発明の効果 本発明を実施する場合には、従来の造粒方法では得られ
なかった次のような効果が得られる。
E1 Effects of the Invention When the present invention is carried out, the following effects that cannot be obtained with conventional granulation methods can be obtained.

(ハ)粒状物の形状2粒径がよくそろう。(計量性。(c) Shape of the granules: 2 particle sizes are well aligned. (Metricability.

流動性、包装性の制御が容易である。)■粒径の変更が
容易である。(粒径毎に多数の型を用意しなくてもよい
。) 0型を使用しなくてすむので、型の清掃、製作等に要す
る費用が不要である。) ◎真空凍結I乾燥により乾燥されるので得られる粒状物
は多孔質で水に対する即溶性があり、有用成分は熱変性
を受けない。
Easy to control fluidity and packaging. )■ Particle size can be easily changed. (There is no need to prepare a large number of molds for each particle size.) Since it is not necessary to use mold 0, there is no need to spend money on mold cleaning, manufacturing, etc. ) Since it is dried by vacuum freeze-drying, the resulting granules are porous and immediately soluble in water, and the useful ingredients are not subject to thermal denaturation.

へ、実施例 実施例11シ せんぶり抽出液の濃縮物(97,2)にデキストリン(
「パインデックス嵐1」(松谷化学工業■)10°Cに
冷却し、内径3+w、外径5朋のガラス管より一30°
C±3°Cに冷却した深さ50αの静かにかくはんした
n−ヘキサン中に静かに滴下し、 500gを造粒した
Examples Example 11 Dextrin (
"Pindex Arashi 1" (Matsuya Chemical Industry ■) Cooled to 10°C, 130° from a glass tube with an inner diameter of 3 + W and an outer diameter of 5 mm.
It was gently dropped into gently stirred n-hexane cooled to ±3°C to a depth of 50α to granulate 500g.

造粒物を金網にて口取し、トレーもすして常法により回
分式の真空凍結乾燥し、  102gの直径3.0〜3
,3朋の略球状の造粒品を得た。
The granules were taken out with a wire mesh, the tray was also drained, and the granules were vacuum freeze-dried in batches using a conventional method to obtain 102 g of 3.0-3.0 g in diameter.
, 3 approximately spherical granules were obtained.

実施例26□ 高麗人参抽出液の濃縮物(餅4.8 )にシヨ糖脂肪酸
エステル帆4%を加え、デキストリン、乳糖1水和物、
アラビアガムの8:21の混合物をx 加温かくはん下に溶解し、Em17.9とした。10″
Cに冷却し、内径1m、外径1.5**のガラス管より
Example 26□ 4% sucrose fatty acid ester was added to a concentrate of ginseng extract (Mochi 4.8), and dextrin, lactose monohydrate,
An 8:21 mixture of gum arabic was dissolved under x heating to give Em 17.9. 10″
from a glass tube with an inner diameter of 1 m and an outer diameter of 1.5**.

−30°C±3°Cに冷却した酢酸エチル、n−ヘキサ
ンの1”l混合液中に滴下造粒した。
The mixture was dropped and granulated into a 1"l mixture of ethyl acetate and n-hexane cooled to -30°C±3°C.

口取し、常法によって真空凍結乾燥し、直径1.8絹の
略球状の粒子を得た。原液1kgより153gの粒状物
を得た。
The sample was sampled and vacuum freeze-dried using a conventional method to obtain approximately spherical particles with a diameter of 1.8 silk. 153 g of granules were obtained from 1 kg of the stock solution.

このものは、実施例1の粒状物同様に60°Cの水に対
し10秒程度で溶解した。
Like the granules in Example 1, this product dissolved in water at 60°C in about 10 seconds.

実施例3 ト1部を水200部に加え、90°C1か(はん下にデ
キストリン、アラビアガム、ソルビトールの3゜乞 12の混合物30部を加えて懸濁さ齢た。40°Cに冷
却し、冷却分別した液状アマニ油を一15°C±2°C
に冷却し、静かにかくはんした状態下に、内径1朋、外
径1.5朋のガラス管より滴下した。金網にて口取し、
冷却したベンジンにてよく洗い、常法にて真空凍結乾燥
し1粒径1.8gm程度の球状粒状物を得た。このもの
は90°Cの熱湯中にて瞬時に崩壊。
Example 3 1 part of dextrin was added to 200 parts of water, and 30 parts of a 30% mixture of dextrin, gum arabic, and sorbitol was added to 90°C and suspended. Cooled to 40°C. The cooled and fractionated liquid linseed oil was heated to 15°C ± 2°C.
The mixture was cooled to a temperature of 1.5 mm, and then dripped into a glass tube with an inner diameter of 1 mm and an outer diameter of 1.5 mm while being gently stirred. Take the mouth with a wire mesh,
The mixture was thoroughly washed with cooled benzene and freeze-dried under vacuum in a conventional manner to obtain spherical particles each having a particle size of about 1.8 gm. This material disintegrates instantly in boiling water at 90°C.

分散した。Dispersed.

実施例4 市販の粉末カラメル([5sJ(大野実業fat))を
固形分30%に熱湯にかくはん溶解した。20″Cに冷
却し、実施例3と同様に造粒し乾燥した。本市は冷水に
投入すると20秒程度で溶解した。
Example 4 Commercially available powder caramel ([5sJ (Ohno Jitsugyo fat)) was dissolved in hot water by stirring to a solid content of 30%. The mixture was cooled to 20''C, granulated and dried in the same manner as in Example 3. When Motoichi was added to cold water, it dissolved in about 20 seconds.

実施例5 ジネブ(エチレンジアミンのビスジチオカルバメイトの
亜鉛塩)の微粉末10部、カオリン微粉末20部、沈降
性炭酸カルシウム末5部、硫酸銅水和物粉末2部、ポリ
エチレングリコール2部、トール油2部、グリセリンモ
ノオレエート1部、ポリビニルアルコール3部、デキス
トリン15部を水150部に激しくかくはん混合し懸濁
した。25°Cに冷却し、実施例2と同様に造粒、乾燥
し、水に即崩壊性の土壌殺菌剤を得た。
Example 5 10 parts of fine powder of zineb (zinc salt of bisdithiocarbamate of ethylenediamine), 20 parts of fine kaolin powder, 5 parts of precipitated calcium carbonate powder, 2 parts of copper sulfate hydrate powder, 2 parts of polyethylene glycol, Thor 2 parts of oil, 1 part of glycerin monooleate, 3 parts of polyvinyl alcohol, and 15 parts of dextrin were mixed and suspended in 150 parts of water with vigorous stirring. The mixture was cooled to 25°C, granulated and dried in the same manner as in Example 2 to obtain a soil fungicide that disintegrates immediately in water.

実施例6 22.0になるまで溶解し15°Cに冷却した。Example 6 It was dissolved until the temperature reached 22.0 and cooled to 15°C.

液体チッ素をデユワ−びんに深さ30口に保持し。Liquid nitrogen is held in a dewar bottle at a depth of 30 openings.

市販の1 mlのメスピペットより滴下造粒した。The mixture was granulated by dropping using a commercially available 1 ml measuring pipette.

粒状物を金網にて口取し、常法にて真空凍結乾燥して2
粒径2.8へ3.11ff程度の水に即溶性の粒状イン
スタント紅茶を得た。
The granules were collected using a wire mesh and vacuum freeze-dried using a conventional method.
A granular instant black tea immediately soluble in water with a particle size of about 2.8 to 3.11 ff was obtained.

、・・’、、!Y \;−1・,...’,,! Y \;-1・

Claims (1)

【特許請求の範囲】 (A)有用成分と、必要ならば賦形剤あるいは結着剤を
含む水溶液を、その水溶液が凍結固化するに充分な低温
に保持された非水和性の液体中に滴下し、凍結造粒する
工程。 (B)かくして得られた凍結造粒物を非水和性の液体よ
り分別する工程。 (C)分別された凍結造粒物を真空凍結乾燥する工程。 以上、(A)、(B)、(C)の三つの工程を結合して
なることを特徴とする造粒方法。
[Scope of Claims] (A) An aqueous solution containing useful ingredients and, if necessary, an excipient or binder, in a non-hydratable liquid kept at a temperature sufficiently low to freeze and solidify the aqueous solution. Dripping and freezing granulation process. (B) A step of separating the thus obtained frozen granules from non-hydratable liquids. (C) A step of vacuum freeze-drying the separated frozen granules. A granulation method characterized by combining the three steps (A), (B), and (C) described above.
JP12290588A 1988-05-18 1988-05-18 Granulating method Pending JPH01293128A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12290588A JPH01293128A (en) 1988-05-18 1988-05-18 Granulating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12290588A JPH01293128A (en) 1988-05-18 1988-05-18 Granulating method

Publications (1)

Publication Number Publication Date
JPH01293128A true JPH01293128A (en) 1989-11-27

Family

ID=14847514

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12290588A Pending JPH01293128A (en) 1988-05-18 1988-05-18 Granulating method

Country Status (1)

Country Link
JP (1) JPH01293128A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5387415A (en) * 1992-01-17 1995-02-07 Alfatec Pharma Gmbh Aloe vera juice containing pellets process for production thereof and the use thereof as pharmaceutical, cosmetic and peroral agents
US5405616A (en) * 1992-01-17 1995-04-11 Alfatec Pharma Gmbh Means for containing active substances, having a shell of hydrophilic macromolecules, active substances and process for preparation thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5387415A (en) * 1992-01-17 1995-02-07 Alfatec Pharma Gmbh Aloe vera juice containing pellets process for production thereof and the use thereof as pharmaceutical, cosmetic and peroral agents
US5405616A (en) * 1992-01-17 1995-04-11 Alfatec Pharma Gmbh Means for containing active substances, having a shell of hydrophilic macromolecules, active substances and process for preparation thereof

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