JP3228288B1 - Method for producing pharmaceutical granule preparation containing branched chain amino acids - Google Patents

Method for producing pharmaceutical granule preparation containing branched chain amino acids

Info

Publication number
JP3228288B1
JP3228288B1 JP2000326514A JP2000326514A JP3228288B1 JP 3228288 B1 JP3228288 B1 JP 3228288B1 JP 2000326514 A JP2000326514 A JP 2000326514A JP 2000326514 A JP2000326514 A JP 2000326514A JP 3228288 B1 JP3228288 B1 JP 3228288B1
Authority
JP
Japan
Prior art keywords
leucine
isoleucine
valine
raw material
solid raw
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2000326514A
Other languages
Japanese (ja)
Other versions
JP2002128668A (en
Inventor
和宏 鷹栖
英俊 坂井
昭 矢吹
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.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
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 Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP2000326514A priority Critical patent/JP3228288B1/en
Priority to PCT/JP2001/009333 priority patent/WO2002034256A1/en
Application granted granted Critical
Publication of JP3228288B1 publication Critical patent/JP3228288B1/en
Publication of JP2002128668A publication Critical patent/JP2002128668A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00Medicinal preparations containing organic active ingredients
    • A61K31/185Acids; Anhydrides, halides or salts thereof, e.g. sulfur acids, imidic, hydrazonic or hydroximic acids
    • A61K31/19Carboxylic acids, e.g. valproic acid
    • A61K31/192Carboxylic acids, e.g. valproic acid having aromatic groups, e.g. sulindac, 2-aryl-propionic acids, ethacrynic acid 
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/14Particulate form, e.g. powders, Processes for size reducing of pure drugs or the resulting products, Pure drug nanoparticles
    • A61K9/16Agglomerates; Granulates; Microbeadlets ; Microspheres; Pellets; Solid products obtained by spray drying, spray freeze drying, spray congealing,(multiple) emulsion solvent evaporation or extraction
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61PSPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P1/00Drugs for disorders of the alimentary tract or the digestive system
    • A61P1/16Drugs for disorders of the alimentary tract or the digestive system for liver or gallbladder disorders, e.g. hepatoprotective agents, cholagogues, litholytics

Landscapes

  • Health & Medical Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • Public Health (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Veterinary Medicine (AREA)
  • Engineering & Computer Science (AREA)
  • Medicinal Chemistry (AREA)
  • General Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Epidemiology (AREA)
  • Medicinal Preparation (AREA)
  • Gastroenterology & Hepatology (AREA)
  • Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
  • Organic Chemistry (AREA)

Abstract

【要約】 【課題】 固形イソロイシン粉砕時の粉塵爆発危険性を
低下させて、イソロイシン、ロイシン及びバリンの3種
のアミノ酸を主薬として含む医薬用顆粒製剤の安全な製
造を可能ならしめる。 【解決手段】 イソロイシン、ロイシン及びバリンを主
薬とする医薬用顆粒製剤を製造する方法において、該3
種の固形原料アミノ酸を粉砕して粒度を調整する工程に
おける固形原料イソロイシンの粉砕を固形原料ロイシン
及び/又は固形原料バリンとの混合粉砕とする医薬用顆
粒製剤の製造方法。
Abstract: PROBLEM TO BE SOLVED: To reduce the risk of dust explosion at the time of pulverizing solid isoleucine, and to make it possible to safely produce a pharmaceutical granule preparation containing three amino acids of isoleucine, leucine and valine as main agents . SOLUTION: In the method for producing a pharmaceutical granule preparation mainly comprising isoleucine, leucine and valine, the method comprises the steps of:
A method for producing a pharmaceutical granule preparation, wherein the solid raw material isoleucine is pulverized with the solid raw material leucine and / or the solid raw material valine in the step of pulverizing a kind of solid raw material amino acid to adjust the particle size.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、イソロイシン、ロ
イシン及びバリンからなる3種の分岐鎖アミノ酸を主薬
(有効成分)として含む医薬用顆粒製剤の製造方法に関
し、特に、該顆粒製剤の造粒原料である3種の分岐鎖ア
ミノ酸の粒子をそれぞれの固体原料から粉砕して調整す
る工程における粉塵爆発の危険を回避するための粉砕方
法に関する。
TECHNICAL FIELD The present invention relates to a method for producing a pharmaceutical granule containing three kinds of branched-chain amino acids consisting of isoleucine, leucine and valine as a main drug (active ingredient), and in particular, to a granulating raw material for the granule. The present invention relates to a pulverization method for avoiding the danger of dust explosion in a step of pulverizing and adjusting particles of three kinds of branched-chain amino acids from respective solid raw materials.

【0002】[0002]

【従来の技術】イソロイシン、ロイシン及びバリンから
なる3種の分岐鎖アミノ酸を主薬として含む医薬用顆粒
製剤は肝疾患に有効な治療薬である。この3種のアミノ
酸を含む顆粒製剤は、顆粒製剤を構成する3種のアミノ
酸の含有量の均一性の保証及び造粒工程における造粒性
の改善のために所定粒度に調整するために粉砕処理され
ている。しかし、これらの3種の分岐鎖アミノ酸の固形
物に限らず、粉砕処理工程では常に粉塵爆発の危険が付
きまとい、その防止対策に多大の設備投資がなされてい
る。上記3種の分岐鎖アミノ酸の場合も例外ではなく、
特にイソロイシンの粉砕処理時における粉塵爆発の危険
が伴うことから、窒素雰囲気下での粉砕、遠隔操作によ
る粉砕、爆発放散口の設置等の安全対策が講じられてい
るのが現状である。
2. Description of the Related Art Pharmaceutical granule preparations containing three kinds of branched-chain amino acids consisting of isoleucine, leucine and valine as a main drug are effective therapeutic agents for liver diseases. The granule preparation containing these three amino acids is subjected to a pulverization treatment in order to adjust the particle size to a predetermined particle size in order to guarantee the uniformity of the contents of the three amino acids constituting the granule preparation and to improve the granulation property in the granulation step. Have been. However, not only the solids of these three kinds of branched-chain amino acids but also the risk of dust explosion is always present in the pulverization process, and a great deal of equipment investment has been made for measures to prevent the explosion. The above three types of branched chain amino acids are no exception,
In particular, since there is a risk of dust explosion during the isoleucine crushing process, safety measures such as crushing under a nitrogen atmosphere, crushing by remote control, and installation of an explosion vent are currently being taken.

【0003】[0003]

【発明が解決しようとする課題】本発明は、肝疾患に対
する有効な治療薬であるイソロイシン、ロイシン及びバ
リンからなる3種の分岐鎖アミノ酸を含有する医薬用顆
粒製剤の製造に使用される該3種のアミノ酸の原料粒子
を調製するために行われるアミノ酸の固形原料の粉砕工
程における粉塵爆発の危険性を回避することができる、
大掛かりな装置を必要としない、安全かつ安価な手段を
提供することを目的とするものである。
DISCLOSURE OF THE INVENTION The present invention relates to a method for producing a granular pharmaceutical preparation containing three kinds of branched-chain amino acids consisting of isoleucine, leucine and valine, which are effective therapeutic agents for liver diseases. It is possible to avoid the danger of dust explosion in the pulverization step of the solid raw material of the amino acid performed to prepare the raw material particles of the seed amino acid,
It is an object of the present invention to provide a safe and inexpensive means that does not require a large-scale device.

【0004】[0004]

【課題を解決するための手段】上記の課題を解決するた
めの本発明は、特に爆発危険性の高い固形イソロイシン
の粉砕時に他の固形ロイシン及び/又は固形バリンから
なる2種の固形アミノ酸の少なくとも1種を混合粉砕す
ることを特徴とする発明であり、さらに以下の発明を包
含する。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention provides a method for producing a solid isoleucine, which has a high risk of explosion, using at least two solid amino acids consisting of other solid leucine and / or solid valine. This invention is characterized by mixing and grinding one kind, and further includes the following inventions.

【0005】(1) 固形イソロイシンを固形ロイシン及び
/又は固形バリンと混合粉砕することを特徴とする、固
形イソロイシンの粉砕方法。
(1) A method for pulverizing solid isoleucine, comprising mixing and pulverizing solid isoleucine with solid leucine and / or solid valine.

【0006】(2) 固形イソロイシンを固形ロイシン及び
/又は固形バリンと混合粉砕することを特徴とする、イ
ソロイシン、ロイシン及びバリンを主薬とする医薬用顆
粒製剤製造用の造粒原料粒子混合物の製造方法。
(2) A method for producing a granulated raw material particle mixture for producing a pharmaceutical granule preparation containing isoleucine, leucine and valine as a main component, comprising mixing and grinding solid isoleucine with solid leucine and / or solid valine. .

【0007】(3)イソロイシン、ロイシン及びバリン
の3種の分岐鎖アミノ酸の固形原料を粉砕して粒度を調
整する工程、次いで該粒度調整した各アミノ酸粒子を含
有する原料を造粒する工程を有するイソロイシン、ロイ
シン及びバリンを主薬とする医薬用顆粒製剤を製造する
方法において、該3種の分岐鎖アミノ酸の固形原料を粉
砕して粒度を調整する工程が、固形原料イソロイシンを
固形原料ロイシン及び/又は固形原料バリンと混して
粉砕することによって固形原料イソロイシンの粉砕時に
おける粉塵爆発の発生を防止するものであることを特徴
とする、イソロイシン、ロイシン及びバリンのみを主薬
とする医薬用顆粒製剤の製造方法。
(3) A step of pulverizing a solid raw material of three kinds of branched-chain amino acids of isoleucine, leucine and valine to adjust the particle size, and then granulating a raw material containing each of the amino acid particles whose particle size has been adjusted. In the method for producing a pharmaceutical granule preparation mainly comprising isoleucine, leucine and valine, the step of pulverizing a solid raw material of the three kinds of branched-chain amino acids to adjust the particle size is performed by converting the solid raw material isoleucine into a solid raw material. during crushing of the solid raw materials isoleucine by <br/> grinding leucine and / or solid raw materials valine and mixed-
A method for producing a pharmaceutical granule preparation comprising only isoleucine, leucine and valine as a principal agent, which is intended to prevent dust explosion from occurring .

【0008】(4) イソロイシン、ロイシン及びバリンの
3種の分岐鎖アミノ酸の固形原料を混合粉砕して造粒用
粒子混合物を調製する工程、次いで該造粒用粒子混合物
を造粒する工程を有することを特徴とする、(3) 項記載
のイソロイシン、ロイシン及びバリンを主薬とする医薬
用顆粒製剤の製造方法。
(4) A step of mixing and pulverizing solid raw materials of three kinds of branched-chain amino acids of isoleucine, leucine and valine to prepare a granulation particle mixture, and then granulating the granulation particle mixture. The method for producing a pharmaceutical granular preparation comprising isoleucine, leucine and valine as a main ingredient according to item (3), which is characterized in that:

【0009】(5) 前記固形原料イソロイシンと固形原料
ロイシン及び/又は固形原料バリンとの混合粉砕は、重
量割合でイソロイシン1に対してロイシン0〜4.4及
びバリン0〜2.6であり、ロイシン及び/又はバリ
ン、好ましくはロイシンとの共存下に行われることを特
徴とする、上記(3) 項又は(4) 項に記載のイソロイシ
ン、ロイシン及びバリンを主薬とする医薬用顆粒製剤の
製造方法。
(5) The mixing and pulverization of the solid raw material isoleucine with the solid raw material leucine and / or the solid raw material valine is such that the weight ratio of leucine 0 to 4.4 and valine 0 to 2.6 with respect to isoleucine 1; Production of a pharmaceutical granule preparation comprising isoleucine, leucine and valine as the main ingredient as described in the above (3) or (4), which is carried out in the presence of leucine and / or valine, preferably leucine. Method.

【0010】(6) 前記固形原料イソロイシンと固形原料
ロイシン及び/又は固形原料バリンとの混合粉砕は、ハ
ンマーミル等の衝撃式(高速回転式)粉砕機、ボールミ
ル等のタンブラー式(媒体式)粉砕機又はジェットミル
等の流体式(気流式)粉砕機による混合粉砕であること
を特徴とする、(1) 項〜(5) 項のいずれか1項に記載の
方法。
(6) The mixing and pulverization of the solid raw material isoleucine with the solid raw material leucine and / or the solid raw material valine is carried out by an impact type (high-speed rotation) pulverizer such as a hammer mill or a tumbler type (medium type) pulverizer such as a ball mill. The method according to any one of items (1) to (5), wherein the mixing and pulverization is performed by a fluid (air flow) pulverizer such as a mill or a jet mill.

【0011】(7) 前記混合粉砕物は、イソロイシン粒子
の粒度が5〜700μm、好ましくは10〜500μm
の範囲とであることを特徴とする、上記(3) 項〜(6) 項
のいずれか1項に記載のイソロイシン、ロイシン及びバ
リンを主薬とする医薬用顆粒製剤の製造方法。
(7) The mixed and pulverized product has a particle size of isoleucine particles of 5 to 700 μm, preferably 10 to 500 μm.
The method for producing a pharmaceutical granule preparation comprising isoleucine, leucine and valine as the main drug according to any one of the above-mentioned items (3) to (6), characterized in that:

【0012】(8) 前記造粒用粒子混合物は、イソロイシ
ン、ロイシン及びバリンの配合割合が重量比で、イソロ
イシン/ロイシン/バリン=1/1.9〜2.2/1.
1〜1.3であることを特徴とする上記(3) 項〜(7) 項
のいずれか1項に記載のイソロイシン、ロイシン及びバ
リンを主薬とする医薬用顆粒製剤の製造方法。
(8) In the granulation particle mixture, isoleucine / leucine / valine = 1 / 1.9 to 2.2 / 1.
Item 1. The method for producing a pharmaceutical granule preparation comprising isoleucine, leucine and valine as the main drug as described in any one of the above items (3) to (7), which is characterized by being 1 to 1.3.

【0013】[0013]

【発明の実施の形態】本発明の各方法における固形原料
イソロイシン、固形原料ロイシン及び固形原料バリン
は、肝疾患に有効な治療薬である該3種の分岐鎖アミノ
酸の粒子を造粒して製造されている医薬用顆粒製剤用の
原料物質として有用なアミノ酸である。
BEST MODE FOR CARRYING OUT THE INVENTION The solid raw material isoleucine, solid raw material leucine and solid raw material valine in each method of the present invention are produced by granulating particles of the three kinds of branched-chain amino acids which are effective therapeutic agents for liver diseases. It is an amino acid useful as a raw material for pharmaceutical granules.

【0014】本発明の医薬用顆粒製剤において、主薬の
一つであるイソロイシンとしては、一般的に発酵法で製
造されている粒度が1mm以下の粒子であり日本薬局方
の規格を満たすものであるが、それに限るものではな
い。それらを5〜700μm、好ましくは10〜500
μmの粒度に調整されたものが使用される。ロイシンと
しては、一般的に発酵法又は抽出法で製造されている粒
度が1mm以下の粒子であり日本薬局方の規格を満たす
ものであるが、それに限るものではない。それらを5〜
700μm、好ましくは10〜500μmの粒度に調整
されたものが使用される。また、バリンとしては、一般
的に発酵法もしくは合成法で製造されている粒度が1m
m以下の粒子であり日本薬局方の規格を満たすものが使
用されるが、それに限るものではない。バリンについて
は局方の規格を満たす限り、その粒度に特に制約はな
い。
In the pharmaceutical granule preparation of the present invention, isoleucine, which is one of the main drugs, is a particle generally produced by a fermentation method and having a particle size of 1 mm or less, which meets the specifications of the Japanese Pharmacopoeia. However, it is not limited to this. They are 5 to 700 μm, preferably 10 to 500
What is adjusted to a particle size of μm is used. Leucine is generally a particle having a particle size of 1 mm or less produced by a fermentation method or an extraction method and satisfies the standards of the Japanese Pharmacopoeia, but is not limited thereto. 5 to them
Particles adjusted to a particle size of 700 μm, preferably 10 to 500 μm are used. In addition, valine generally has a particle size of 1 m produced by a fermentation method or a synthesis method.
Particles having a particle size of m or less and satisfying the standards of the Japanese Pharmacopoeia are used, but not limited thereto. There is no particular limitation on the particle size of valine as long as it meets the specifications of the Pharmacopoeia.

【0015】ここでいう混合粉砕とは、イソロイシン、
ロイシン及びバリンを予め混合した後に粉砕する方法、
又はイソロイシン、ロイシン及びバリンを混合しながら
粉砕する方法いずれでも良い。
[0015] The mixed pulverization here means isoleucine,
A method in which leucine and valine are premixed and then crushed,
Alternatively, any method of pulverizing while mixing isoleucine, leucine and valine may be used.

【0016】ここでいう混合とはコンテナ式混合機等の
容器回転型混合機、流動層型混合機等のエアー撹拌型混
合機、撹拌羽根及び撹拌リボンの回転による撹拌混合
機、粉体輸送ライン中で混合するライン混合機、粉砕機
等の原料供給口に設置されるフィーダー型混合機による
混合が好ましいが、特に限定されるものでは無い。
The term "mixing" as used herein means a container rotary mixer such as a container mixer, an air stirring mixer such as a fluidized bed mixer, a stirring mixer by rotating stirring blades and a stirring ribbon, and a powder transport line. Mixing by a feeder type mixer installed at a raw material supply port such as a line mixer or a pulverizer for mixing in the inside is preferable, but not particularly limited.

【0017】ここでいう粉砕とは、ハンマーミル等の衝
撃式(高速回転式)粉砕機、ボールミル等のタンブラー
式(媒体式)粉砕機又はジェットミル等の流体式(気流
式)粉砕機による粉砕が好ましいが、特に限定されるも
のでは無い。
The term "pulverization" as used herein refers to pulverization using an impact (high-speed rotation) pulverizer such as a hammer mill, a tumbler (medium type) pulverizer such as a ball mill, or a fluid (pneumatic) pulverizer such as a jet mill. Is preferred, but is not particularly limited.

【0018】本発明の顆粒製剤におけるイソロイシン、
ロイシン及びバリンの配合割合は重量比で、イソロイシ
ン/ロイシン/バリン=1/1.9〜2.2/1.1〜
1.3である。
Isoleucine in the granular preparation of the present invention,
The mixing ratio of leucine and valine is isoleucine / leucine / valine = 1 / 1.9 to 2.2 / 1.1.
1.3.

【0019】本発明の顆粒製剤の製造に際しては、結合
剤を使用することができる。結合剤としては、メチルセ
ルロース、ヒドロキシプロピルセルロース、ヒドロキシ
プロピルメチルセルロース、ヒドロキシプロピルメチル
セルロースフタレート等のセルロース誘導体、トウモロ
コシデンプン、コムギデンプン等のデンプン類、ポリビ
ニルピロリドン、アクリス酸ポリマーなどの合成高分子
類、アラビアゴム、ゼラチン等の天然高分子類等の日本
薬局方あるいは医薬品添加物規格等の規格を満たしてい
る医薬用として使用できるものであれば特に制限なく使
用できる。また、その使用量も通常の造粒が可能な範囲
である。
In producing the granular preparation of the present invention, a binder can be used. As the binder, methylcellulose, hydroxypropylcellulose, hydroxypropylmethylcellulose, cellulose derivatives such as hydroxypropylmethylcellulose phthalate, corn starch, starches such as wheat starch, polyvinylpyrrolidone, synthetic polymers such as acrylic acid polymer, gum arabic, Any polymer can be used without particular limitation as long as it can be used as a medicinal product satisfying the standards such as the Japanese Pharmacopoeia or excipient standards such as natural polymers such as gelatin. Also, the amount used is within the range in which normal granulation is possible.

【0020】本発明の医薬用顆粒製剤における前記3種
の分岐鎖アミノ酸粒子を含む顆粒剤は、高速攪拌造粒
機、流動層造粒機、プラネタリーミキサー、乾式圧扁造
粒機、破砕造粒機、押出し造粒機、転動造粒機、噴霧乾
燥造粒機、コーティング造粒機のどの機器を使用しても
作ることができるが、高速攪拌造粒機、押し出し造粒機
が好ましい。押出し造粒法とは可塑性を付与された粉末
を多数の穴のあいたスクリーンから押し出すことにより
造粒する方法であり、前押し出し式造粒機、ディスクペ
レッター式造粒機、リングダイ式造粒機、バスケット式
造粒機、オシレーティング式造粒機、シリンダー式造粒
機等が使用される。
The granules containing the three kinds of branched-chain amino acid particles in the pharmaceutical granule of the present invention may be a high-speed stirring granulator, a fluidized bed granulator, a planetary mixer, a dry pressing granulator, a crushing granulator. Granulation machine, extrusion granulator, tumbling granulator, spray drying granulator, and coating granulator can be used, but high-speed stirring granulator and extrusion granulator are preferred. . Extrusion granulation is a method of granulating by extruding plasticized powder through a screen with many holes, pre-extrusion granulator, disk pelletizer granulator, ring die granulator. Machine, basket type granulator, oscillating type granulator, cylinder type granulator and the like are used.

【0021】高速攪拌造粒法とは、粉に水あるいはバイ
ンダー液を投入あるいは噴霧し、攪拌羽根の回転により
せん断・転動・圧密化を行い造粒する方法であり竪型・
横型の攪拌造粒機が使用される。流動層造粒法とは、粉
を流動しながら水あるいはバインダー液を噴霧し、粉を
凝集させることにより行われる造粒法であり、流動層型
造粒機、攪拌流動層型造粒機、転動流動層型造粒機、攪
拌転動流動層型造粒機が使用される。
The high-speed stirring granulation method is a method in which water or a binder liquid is charged or sprayed into powder, and the powder is subjected to shearing / rolling / consolidation by rotation of a stirring blade to perform granulation.
A horizontal stirring granulator is used. The fluidized bed granulation method is a granulation method performed by spraying water or a binder liquid while flowing the powder, and aggregating the powder.A fluidized bed granulator, a stirred fluidized bed granulator, A tumbling fluidized bed type granulator and a stirring tumbling fluidized bed type granulator are used.

【0022】乾式圧扁造粒法とは水あるいはバインダー
液を使用せず粉を圧縮して成形する方法であり、ロール
プレス、ブリケッティングマシン、単発式打錠機、ロー
タリー式打錠機が使用される。転動造粒法とは、粉末を
転がして造粒する方法のことであり、ドラム型造粒機、
皿型造粒機、振動造粒機、円盤回転式造粒機が使用され
る。
The dry pressing granulation method is a method of compressing and molding a powder without using water or a binder liquid, and includes a roll press, a briquetting machine, a single-shot tableting machine, and a rotary tableting machine. used. The rolling granulation method is a method of rolling and granulating powder, and a drum-type granulator,
Dish-type granulators, vibratory granulators, and rotary disk granulators are used.

【0023】[0023]

【実施例】次に、実施例を挙げて本発明をより具体的に
説明するが、本発明は以下の実施例によって限定される
ものではない。
EXAMPLES Next, the present invention will be described more specifically with reference to examples, but the present invention is not limited to the following examples.

【0024】実施例1 3種の分岐鎖アミノ酸(ロイシン、イソロイシン、バリ
ン)をそれぞれ単品で粉砕した粉砕物と3種の分岐鎖ア
ミノ酸を混合した後に粉砕した混合粉砕物の粉塵爆発性
を比較した。爆発危険度は単品粉砕ではロイシンがクラ
スII、イソロイシンがクラスI でバリンがクラスIIであ
ったが、混合粉砕物はクラスIIになり、3種類をそれぞ
れ単品で粉砕するよりも混合して粉砕する方が爆発危険
度が著しく低下することが分かった。
Example 1 The dust explosive properties of three types of branched-chain amino acids (leucine, isoleucine, and valine), each of which was individually pulverized, mixed with three types of branched-chain amino acids, and then pulverized, were compared. . The explosion risk was as follows: In the case of single-piece grinding, leucine was class II, isoleucine was class I, and valine was class II, but the mixed and crushed product was class II. It was found that the risk of explosion was significantly reduced.

【0025】なお、クラス別爆発対策は以下のとおりで
ある。 クラス特I:窒素パージ必要、 クラスI:爆発放散口等の防爆対策必要 クラスII:アース設置 クラスIII :対策必要なし 3種の分岐鎖アミノ酸に対する粉塵爆発性評価結果を表
1及び図1にまとめて示す。
The explosion countermeasures for each class are as follows. Class I: Nitrogen purge required, Class I: Explosion-proof measures such as explosion vents required Class II: Ground installation Class III: No measures required Table 1 and Figure 1 summarize the dust explosion evaluation results for three types of branched-chain amino acids. Shown.

【0026】[0026]

【表1】 [Table 1]

【0027】[0027]

【発明の効果】以上の結果から明らかなように、本発明
の3種のアミノ酸の混合粉砕法によれば、その粉砕工程
における粉塵爆発性を大幅に低下させることができ、そ
の結果、該3種のアミノ酸を含む本発明の肝疾患治療薬
である医薬用顆粒製剤の製造を安全に実施することを可
能ならしめるものである。
As is evident from the above results, according to the method of the present invention for mixing and grinding three kinds of amino acids, dust explosion in the grinding step can be greatly reduced. Thus, it is possible to safely carry out the production of a pharmaceutical granule preparation which is a therapeutic agent for liver disease of the present invention and contains various amino acids.

【図面の簡単な説明】[Brief description of the drawings]

【図1】3種の分岐鎖アミノ酸(ロイシン、イソロイシ
ン、バリン)粉砕物の粉塵爆発性を示す図である。
FIG. 1 is a view showing the dust explosive properties of a ground product of three types of branched-chain amino acids (leucine, isoleucine, and valine).

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平8−198748(JP,A) (58)調査した分野(Int.Cl.7,DB名) A61K 31/198 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-8-198748 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) A61K 31/198

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 イソロイシン、ロイシン及びバリンの3
種の固形原料アミノ酸を粉砕して粒度を調整する工程、
次いで該粒度調整した各アミノ酸粒子を含有する原料を
造粒する工程を有する、イソロイシン、ロイシン及びバ
リンの配合割合が重量比でイソロイシン/ロイシン/バ
リン=1/1.9〜2.2/1.1〜1.3であるイソ
ロイシン、ロイシン及びバリンのみを主薬とする医薬用
顆粒製剤を製造する方法において、該3種の固形原料ア
ミノ酸を粉砕して粒度を調整する工程が、固形原料イソ
ロイシンを固形原料ロイシン及び/又は固形原料バリン
と混して粉砕することによって固形原料イソロイシン
の粉砕時における粉塵爆発の発生を防止するものである
ことを特徴とする、医薬用顆粒製剤の製造方法。
The present invention relates to isoleucine, leucine and valine.
A process of adjusting the particle size by crushing the seed solid amino acid,
Next, a step of granulating a raw material containing each of the amino acid particles whose particle size has been adjusted is performed. The mixing ratio of isoleucine, leucine, and valine is isoleucine / leucine / valine = 1 / 1.9 to 2.2 / 1. In the method for producing a pharmaceutical granule preparation containing only isoleucine, leucine and valine as the main drug, the step of pulverizing the three solid amino acids to adjust the particle size, the method comprises the steps of:
Leucine as solid raw material leucine and / or solid raw material valine
Solid raw materials isoleucine by to mixed-to Milling
A method for producing a pharmaceutical granule, which is intended to prevent dust explosion during pulverization .
【請求項2】 前記固形原料イソロイシンと固形原料ロ
イシン及び/又は固形原料バリンとの混合粉砕は、重量
割合でイソロイシン1に対して、ロイシン0〜4.4及
びバリン0〜2.6の混合粉砕であることを特徴とする
請求項1記載の医薬用顆粒製剤の製造方法。
2. The mixing and grinding of the solid raw material isoleucine and the solid raw material leucine and / or the solid raw material valine is performed by mixing and grinding leucine 0 to 4.4 and valine 0 to 2.6 with respect to isoleucine 1 in a weight ratio. The method for producing a pharmaceutical granule preparation according to claim 1, wherein:
【請求項3】 前記固形原料イソロイシンと固形原料ロ
イシン及び/又は固形原料バリンとの混合粉砕は、ハン
マーミル等の衝撃式(高速回転式)粉砕機、ボールミル
等のタンブラー式(媒体式)粉砕機又はジェットミル等
の流体式(気流式)粉砕機による混合粉砕であることを
特徴とする、請求項1又は2に記載の医薬用顆粒製剤の
製造方法。
3. The mixing and grinding of the solid raw material isoleucine and the solid raw material leucine and / or the solid raw material valine is performed by a shock (high-speed rotation) pulverizer such as a hammer mill or a tumbler (medium type) pulverizer such as a ball mill. 3. The method for producing a pharmaceutical granule preparation according to claim 1, wherein the pulverization is performed by mixing and pulverization using a fluid (air flow) pulverizer such as a jet mill.
JP2000326514A 2000-10-26 2000-10-26 Method for producing pharmaceutical granule preparation containing branched chain amino acids Expired - Lifetime JP3228288B1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2000326514A JP3228288B1 (en) 2000-10-26 2000-10-26 Method for producing pharmaceutical granule preparation containing branched chain amino acids
PCT/JP2001/009333 WO2002034256A1 (en) 2000-10-26 2001-10-24 Process for producing granular drug preparation containing branched amino acids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000326514A JP3228288B1 (en) 2000-10-26 2000-10-26 Method for producing pharmaceutical granule preparation containing branched chain amino acids

Publications (2)

Publication Number Publication Date
JP3228288B1 true JP3228288B1 (en) 2001-11-12
JP2002128668A JP2002128668A (en) 2002-05-09

Family

ID=18803687

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000326514A Expired - Lifetime JP3228288B1 (en) 2000-10-26 2000-10-26 Method for producing pharmaceutical granule preparation containing branched chain amino acids

Country Status (2)

Country Link
JP (1) JP3228288B1 (en)
WO (1) WO2002034256A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3211824B1 (en) * 2000-10-26 2001-09-25 味の素株式会社 Pharmaceutical granule preparation containing branched-chain amino acid and method for producing the same
EP1839502A4 (en) * 2004-12-07 2010-03-24 Ajinomoto Kk Fine powder of amino acid and suspension thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1177384B (en) * 1984-12-12 1987-08-26 Boeehringer Biochemia Robin Sp DIETARY GRANULAR PRODUCTS BASED ON AMINO ACIDS AND PROCEDURE FOR THEIR PREPARATION
JP3617102B2 (en) * 1995-01-27 2005-02-02 味の素株式会社 Amino acid nutritional composition with an early recovery effect on human muscle fatigue

Also Published As

Publication number Publication date
WO2002034256A1 (en) 2002-05-02
JP2002128668A (en) 2002-05-09

Similar Documents

Publication Publication Date Title
EP1565258B1 (en) Process and apparatus for continuous wet granulation of powder material
US20160256390A1 (en) Process for producing cellulose derivatives of high bulk density and good flowability
JP3368898B1 (en) Process for producing granules containing branched chain amino acids
CA3023478C (en) Method for manufacturing acetaminophen preparation
JPS6191118A (en) Granule of thiamine salt, its production, and tablet
JP3165700B2 (en) High-speed stirring granulation method and high-speed stirring granulator
CN103705520A (en) Method for preparing rivaroxaban solid composition
JP3211824B1 (en) Pharmaceutical granule preparation containing branched-chain amino acid and method for producing the same
CN103705510A (en) Method for preparing azilsartan solid composition
JPH05320045A (en) Spray drying method for manufacturing medicine powder composition being compressable directly to tablet
JP3228288B1 (en) Method for producing pharmaceutical granule preparation containing branched chain amino acids
JP7106161B2 (en) Methods for treating drug substance particles with irregular particle sizes
CN109718215A (en) A kind of Ezetimibe piece
Sharma et al. Review on Moisture activated Dry Granulation Process
CN107875129A (en) A kind of Ezetimibe atorvastatin preparation method
JPS63117905A (en) Granular tricalcium phosphate composition proper for directly forming compressed tablet
JP4100723B2 (en) Granule and its production method
JPH02255613A (en) Pharmaceutical containing dioctyl sodium sulfosuccinate blended therein
CN114105839A (en) Pretreatment method of bulk drug and composition thereof
CN112190580A (en) Method for preparing ezetimibe tablets and ezetimibe tablets
JP3228289B1 (en) Method for producing pharmaceutical granules containing branched-chain amino acids
JPS5849428A (en) Production of fine granular material
CN118717690A (en) Hydrobromic acid voltammetric acid tablet and preparation method thereof
JP2017165724A (en) Solid preparation containing alkyl cellulose and method of producing the same

Legal Events

Date Code Title Description
TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20010807

R150 Certificate of patent or registration of utility model

Ref document number: 3228288

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R154 Certificate of patent or utility model (reissue)

Free format text: JAPANESE INTERMEDIATE CODE: R154

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100907

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100907

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100907

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110907

Year of fee payment: 10

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110907

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120907

Year of fee payment: 11

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120907

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130907

Year of fee payment: 12

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term