JPS6365372B2 - - Google Patents

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Publication number
JPS6365372B2
JPS6365372B2 JP58037913A JP3791383A JPS6365372B2 JP S6365372 B2 JPS6365372 B2 JP S6365372B2 JP 58037913 A JP58037913 A JP 58037913A JP 3791383 A JP3791383 A JP 3791383A JP S6365372 B2 JPS6365372 B2 JP S6365372B2
Authority
JP
Japan
Prior art keywords
roll
gear
granulator
granulation
dry granulation
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
Application number
JP58037913A
Other languages
Japanese (ja)
Other versions
JPS59162937A (en
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 filed Critical
Priority to JP3791383A priority Critical patent/JPS59162937A/en
Publication of JPS59162937A publication Critical patent/JPS59162937A/en
Publication of JPS6365372B2 publication Critical patent/JPS6365372B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は医薬品、農薬、食品等の業界で広く使
用されている乾式造粒装置の改良に関し、対をな
すロールの片方のロールの表面に複数列の円周を
とりまく三角柱状隆起を設けたロール式圧縮成形
装置、ギヤー式粗砕製粒装置およびロール・グラ
ニユレーターの組合せからなる乾式造粒装置に関
する。 水で分解され易い成分を含有する粉末を製粒す
る方法である乾式造粒法として一般的にロール圧
縮成形および製粒装置が用いられている。 図1はこの一例で、供給ホツパー1内の粉末2
は垂直スクリユー3で成形ロール4―a,4―b
に押し込まれ、粉末2を成形するのに最適な圧力
で圧縮されて板状成形物5になる。この板状成形
物5をローター式粉砕装置(ローター6とパンチ
ングプレート7で構成)を用いてローター6の回
転衝撃力で破砕すると共に、その回転遠心力によ
つてパンチングプレート7に破砕物をこすりつ
け、その穴を通過させる事によつて、所定の粗顆
粒8が得られる。更に、ロール・グラニユレータ
ーと通称されているロール型破砕装置、即ち、切
口の断面が三角形の縦溝を有する3段のローラー
9―1―a,9―1―b,9―2―a,9―2―
b,9―3―a,9―3―b(図3に1段のロー
ラーを示したが、溝ピツチPが、例えば3段ロー
ルの上段から順に3mm,2mm,1mm)を通す事に
よつて顆粒10が得られる。なお、物性や必要と
する顆粒の大きさによつては、2段のローラー9
―1―a,9―1―b,9―2―a,9―2―b
で設備対応を取る場合もある。又、この顆粒10
の中には、粗砕或いは製粒時に生じた微粉末が含
まれているので、一般には篩過装置で分級し、微
粉末を供給ホツパー1に戻して再使用する。 以上の従来から使用されている装置には、下記
の欠点を有していた。 1 微粉末が多く発生してしまう為、処理能力の
低下や粉末付着トラブルが起り易い。その理由
は主に2つが考えられる。 成形ロール4―a,4―bは図2に示した
構造であり、その板状成形物5は成形圧力伝
達や粉末供給のバラツキを受け易く、中央部
が硬く、両端部が軟らかくなる。その為、粗
砕および製粒時において、最適条件での運転
維持が困難である。 大きな容積を有する板状成形物を、小さな
容積の顆粒にする方法として、粗砕物をロー
ラーの衝撃と、その遠心力によるパンチング
プレート7へのこすりつけという微粉末の発
生が多い方法にだけ依存している。 なお、大型機では板状成形物5の板幅が大
きくなるので、一層重大な欠点となつてい
る。 2 3段のローラー9―1―a,,9―1―b,
9―2―a,9―2―b,9―3―a,9―3
―bから成る製粒機は前述した様に、三角形状
の縦溝の溝ピツチPが小さく、しかも、相対す
るローラーの溝間隔が製粒に重要な要因となる
為、高い製作精度が必要となる。その為、設備
費が非常に高い。一方、運転時には縦溝の谷部
に粉末の付着が生じる為、現状では一般的に板
状のスクレツパーを用いて除去している。しか
し、構造上高い精度が困難であり、又、必らず
しもその効果が得られていない。 かかる従来装置の改良を目的として鋭意検討し
た結果得られたのが本発明装置である。 以下、図面に基づき本発明を説明する。 図4は本発明のロール式圧縮成形装置の改良成
形ロールの平立面図を示し、図5は図4のロール
によつて得られた成形物の平断面図を示す。図4
に示される如く、本発明においては一対のロール
の片方のロール成形面に複数列の円周をとりまく
三角柱状隆起12を設けてある。該隆起12は正
三角形又はそれに近い形状が効果的であり、ロー
ル成形面上に設ける間隔は等間隔が好ましく、隆
起物のピツチBは目的とする造粒物の大きさによ
つて異なるが、医薬品業界における造粒を考慮
し、かつ製作精度を考慮した場合、約1〜6mm
(4mmで効果確認)が好ましい。 かかる本発明のロール式圧縮成形装置を使用す
ると図5の形状の板状成形物が得られる。今回実
施したピツチB=4mmの場合T1=1.2mmに対しT2
=0.3〜0.4mmと隆起に対応する部分は非常に薄く
なり下記する図6のギヤー式粗砕製粒装置にかけ
るとシヨツクでT2部分が切れ、恰も“ひもかわ
うどん”と呼ばれる麺状成形物を整列させて粗砕
する如く、良好な粗顆粒が得られる。 なお、図5の板状成形物の断面は、その全体に
わたつてほぼ同一の麺状断面を有しており、換言
すれば図4の三角柱状隆起12によつて、板状成
形物は成形圧力伝達や粉末供給のバラツキを受け
にくくなるので、均一成形化が実現でき、前記の
従来型乾式造粒装置の欠点1が改善できる。 図6は2本のギヤー13―a,13―bを並行
に配置したギヤー式粗砕製粒装置の機構図で両ギ
ヤーのギヤー歯の山間隔kが板状成形物の厚さ
T1の3/4以内に調整してある。なお、ギヤー歯は 山同士を向い合わせても山―谷の様にずらしても
良いが、山同士を組み合わせた方が特に効果的で
ある。 本装置は機構的には剪断力を利用している為微
粉末の発生が非常に少なく、又、同一波形のかき
取り用ギヤー14をギヤー13―a,13―b
(図6ではギヤー13―a側だけ描いてある。)に
かみ合わせる事によつて、ギヤー13―a,13
―bの付着物を除去でき、安定した粗顆粒を生産
できる。但し、ギヤー13―a,13―bとかき
取り用ギヤー14とは、摩耗を防止する為、適当
なギヤー間のクリアランスを設けて保持すること
もできる。なお、かき取り用ギヤー14はシリン
ダー又はカム機構等公知の方法による矢印Sに示
した往復運動を行う軸15にベアリングを介して
組み込んでおり、ギヤー13―a,13―bのギ
ヤー歯全面に周期的に行きわたる様になつてい
る。又、ギヤー13―a,13―bおよびかき取
り用ギヤー14のギヤー歯は、図7のイ,ロに示
した形状等が考えられ、特にロにより良好な結果
が得られている。 好ましいP1,θ1,t1,P2,θ2およびt2は表1の
とおりである。
The present invention relates to an improvement of a dry granulation device that is widely used in the pharmaceutical, agrochemical, food, and other industries. The present invention relates to a dry granulation device consisting of a combination of a type compression molding device, a gear type coarse granulation device, and a roll granulator. Roll compression molding and granulation equipment are generally used as a dry granulation method, which is a method of granulating powder containing components that are easily decomposed by water. Figure 1 shows an example of this, with powder 2 in supply hopper 1.
Forming rolls 4-a, 4-b with vertical screw 3
The powder 2 is pressed into the powder 2 and compressed with the optimum pressure to form a plate-shaped molded product 5. This plate-shaped molded product 5 is crushed by the rotational impact force of the rotor 6 using a rotor-type crusher (consisting of a rotor 6 and a punching plate 7), and the crushed material is rubbed against the punching plate 7 by the rotational centrifugal force. By passing through the holes, predetermined coarse granules 8 can be obtained. Furthermore, a roll-type crushing device commonly known as a roll granulator, that is, three stages of rollers 9-1-a, 9-1-b, 9-2-a, each having vertical grooves with a triangular cut section, is used. ,9-2-
b, 9-3-a, 9-3-b (Figure 3 shows a single-stage roller, but the groove pitch P is, for example, 3 mm, 2 mm, and 1 mm from the top of the 3-stage roll). Granules 10 are obtained. Note that depending on the physical properties and the required size of the granules, two-stage rollers 9 may be used.
-1-a, 9-1-b, 9-2-a, 9-2-b
In some cases, equipment measures may be taken. Also, this granule 10
Since the powder contains fine powder generated during coarse crushing or granulation, it is generally classified using a sieving device, and the fine powder is returned to the supply hopper 1 for reuse. The conventionally used devices described above have the following drawbacks. 1. Since a large amount of fine powder is generated, processing capacity is reduced and problems with powder adhesion are likely to occur. There are two main reasons for this. The molding rolls 4-a and 4-b have the structure shown in FIG. 2, and the plate-shaped molded product 5 thereof is susceptible to variations in molding pressure transmission and powder supply, and is hard at the center and soft at both ends. Therefore, it is difficult to maintain operation under optimal conditions during coarse crushing and granulation. As a method for converting a plate-like molded product having a large volume into granules having a small volume, the method relies only on a method that generates a large amount of fine powder, in which the crushed material is rubbed against the punching plate 7 by the impact of a roller and the resulting centrifugal force. There is. In addition, in a large-sized machine, the width of the plate-shaped molded product 5 becomes large, and this becomes an even more serious drawback. 2 Three stages of rollers 9-1-a, 9-1-b,
9-2-a, 9-2-b, 9-3-a, 9-3
As mentioned above, the granulator consisting of B has a small groove pitch P of the triangular vertical grooves, and the groove spacing between opposing rollers is an important factor in granulation, so high manufacturing precision is required. Become. Therefore, equipment costs are extremely high. On the other hand, during operation, powder adheres to the troughs of the vertical grooves, so currently a plate-shaped scraper is generally used to remove it. However, it is difficult to achieve high precision due to its structure, and the effect is not always achieved. The device of the present invention was obtained as a result of intensive studies aimed at improving such conventional devices. The present invention will be explained below based on the drawings. FIG. 4 shows a plan elevational view of an improved forming roll of the roll-type compression molding apparatus of the present invention, and FIG. 5 shows a plan sectional view of a molded product obtained by the roll of FIG. 4. Figure 4
As shown in the figure, in the present invention, a plurality of rows of circumferential triangular prism-shaped ridges 12 are provided on the forming surface of one of the pair of rolls. It is effective for the ridges 12 to have an equilateral triangular shape or a shape close to it, and the intervals provided on the roll forming surface are preferably equal intervals, and the pitch B of the ridges varies depending on the size of the target granulated product. Considering granulation in the pharmaceutical industry and manufacturing accuracy, approximately 1 to 6 mm.
(Effect confirmed at 4 mm) is preferable. When the roll-type compression molding apparatus of the present invention is used, a plate-shaped molded product having the shape shown in FIG. 5 can be obtained. In the case of pitch B = 4 mm, T 1 = 1.2 mm and T 2
= 0.3 to 0.4 mm, the part corresponding to the bumps is very thin, and when it is applied to the gear-type coarse granulation machine shown in Figure 6 below, the T 2 part is cut off by the shot, forming a noodle shape called "Himokawa Udon". Good coarse granules can be obtained by aligning and crushing the particles. The cross section of the plate-shaped molded product in FIG. Since it is less susceptible to variations in pressure transmission and powder supply, uniform molding can be achieved and the drawback 1 of the conventional dry granulation apparatus described above can be improved. Figure 6 is a mechanical diagram of a gear-type coarse crushing and granulating device in which two gears 13-a and 13-b are arranged in parallel.The distance k between the gear teeth of both gears is the thickness of the plate-shaped molded product
Adjusted to within 3/4 of T 1 . The gear teeth may be arranged with the peaks facing each other or offset like peaks and valleys, but it is particularly effective to combine the peaks. Mechanically, this device uses shearing force, so there is very little generation of fine powder.
(Only the gear 13-a side is shown in Figure 6.) By meshing with the gears 13-a and 13,
-B deposits can be removed and stable coarse granules can be produced. However, the gears 13-a, 13-b and the scraping gear 14 may be held with an appropriate clearance between them to prevent wear. The scraping gear 14 is incorporated via a bearing into a shaft 15 that performs reciprocating motion as indicated by the arrow S using a known method such as a cylinder or cam mechanism, and the scraping gear 14 is installed on the entire surface of the gear teeth of the gears 13-a and 13-b. It seems to be prevalent periodically. Further, the gear teeth of the gears 13-a, 13-b and the scraping gear 14 may have the shapes shown in A and B of FIG. 7, and particularly good results have been obtained with B. Preferable P 1 , θ 1 , t 1 , P 2 , θ 2 and t 2 are as shown in Table 1.

【表】 次に、図4の改良成形ロールと図6のギヤー式
粗砕製粒装置を併用する事によつて、前述の様に
粗顆粒が安定になり、その結果、一般的には従来
3段必要であつた図1の製粒機は2段のロール9
―2―a,9―2―b,9―3―a,9―3―b
又は粉末物性によつては1段のロール9―3―
a,9―3―bに設備軽減できる。 更に必要とする顆粒の大きさによつては、今回
開発のギヤー式粗砕製粒装置を2段ないし3段設
ける事によつて、従来の非常に高価な製粒機を用
いないで顆粒を得る事ができ、いずれも大きな収
率アツプと設備費の軽減が可能となる。 表2に従来型乾式造粒装置による顆粒および今
回発明の装置による顆粒の分布表を記す。
[Table] Next, by using the improved forming roll shown in Fig. 4 together with the gear-type coarse granulation device shown in Fig. 6, the coarse granules become stable as described above, and as a result, generally the The granulator in Figure 1, which required three stages, has two rolls 9.
-2-a, 9-2-b, 9-3-a, 9-3-b
Or one stage roll 9-3- depending on powder physical properties
Equipment can be reduced to a, 9-3-b. Furthermore, depending on the size of the granules required, by installing two or three stages of the newly developed gear-type coarse granulator, it is possible to produce granules without using a conventional very expensive granulator. In both cases, it is possible to greatly increase yield and reduce equipment costs. Table 2 shows the distribution of granules produced by the conventional dry granulation apparatus and the granules produced by the apparatus of the present invention.

【表】 付着物のかき取り方法につき更に説明を加え
る。 図6でギヤー式ロールに対する方法につき説明
したが、従来の製粒機として使用している図1の
縦溝ロールに対しても、図8および図9に示した
様に、縦溝ギヤー歯と同一のギヤー歯に切欠17
を有したかき取り用縦ギヤーロール16をかみ合
わせる事(両ロールのギヤー歯および切欠の摩耗
を考慮して適当なクリアランスを保持する場合も
ある。)によつて、付着物のかき取りが可能とな
る。なお、図8および図9にはロール9―1―a
に対するかき取り用縦ギヤーロール16のみを描
いてあるが、ロール9―1―bについても同様で
ある。更に図1のロール9―2―a,9―2―
b,9―3―a,9―3―bについても同様であ
る事については説明を加えるまでもない。 以上の様に本発明による装置によつて、従来の
乾式造粒装置が有していた前記欠点はいずれも解
決できる。
[Table] Add further explanation on how to scrape off deposits. Although the method for the gear type roll was explained in Fig. 6, the method for the vertically grooved roll shown in Fig. 1 used as a conventional granulator can also be applied to the vertically grooved gear teeth as shown in Figs. 8 and 9. Notch 17 on the same gear tooth
It is possible to scrape off deposits by meshing the vertical gear rolls 16 for scraping, each having an appropriate clearance (an appropriate clearance may be maintained in consideration of the wear of the gear teeth and notches of both rolls). becomes. In addition, in FIGS. 8 and 9, the roll 9-1-a
Although only the vertical gear roll 16 for scraping is shown, the same applies to the roll 9-1-b. Furthermore, the rolls 9-2-a, 9-2- in Fig. 1
There is no need to explain that the same applies to b, 9-3-a, and 9-3-b. As described above, the apparatus according to the present invention can solve all of the above-mentioned drawbacks of the conventional dry granulation apparatus.

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

図1は従来の乾式ロール造粒装置の斜視図、図
2は従来の成形ロールの平立面図、図3はロー
ル・グラニユレーターの1段分の縦溝ロールを表
した平立面図、図4は本発明による改良成形ロー
ルの平立面図、図5は図4の改良成形ロールによ
つて得られた成形物の平断面図、図6は本発明に
よるギヤー式粗砕製粒装置およびかき取りギヤー
装置の斜視図、図7は図6の装置におけるギヤー
歯を表わした立面図、図8は縦溝ロールに対する
かき取り用ギヤー装置の機構を表わした斜視図、
及び図9は図8の一部分を表わした平断面図であ
る。
Fig. 1 is a perspective view of a conventional dry roll granulation device, Fig. 2 is a plan elevation view of a conventional forming roll, and Fig. 3 is a plan elevation view showing one stage of fluted rolls of a roll granulator. , FIG. 4 is a plan elevational view of the improved forming roll according to the present invention, FIG. 5 is a plan cross-sectional view of a molded product obtained by the improved forming roll of FIG. 4, and FIG. 6 is a gear type coarse granulation granulator according to the present invention. A perspective view of the device and the scraping gear device, FIG. 7 is an elevational view showing the gear teeth in the device of FIG. 6, FIG. 8 is a perspective view showing the mechanism of the scraping gear device for the fluted roll,
9 is a plan cross-sectional view showing a portion of FIG. 8.

Claims (1)

【特許請求の範囲】 1 対をなすロールの片方のロールの表面に複数
列の円周をとりまく三角柱状隆起を設けたロール
式圧縮成型装置、ギヤー式粗砕製粒装置およびロ
ール・グラニユレーターとの組合せからなる乾式
造粒装置。 2 ギヤー式粗砕製粒装置のギヤー溝部に、左右
往復可能な付着物除去用ギヤーを組込んだ特許請
求の範囲第1項記載の乾式造粒装置。 3 ロール・グラニユレーターの縦溝ロールの溝
部に付着物除去用ギヤーを組込んだ特許請求の範
囲第1項記載の乾式造粒装置。
[Claims] A roll-type compression molding device, a gear-type coarse crushing and granulating device, and a roll granulator, in which a plurality of rows of triangular prism-shaped ridges surrounding the circumference are provided on the surface of one roll of a pair of rolls. A dry granulation device consisting of a combination of 2. The dry granulation device according to claim 1, wherein a gear for removing deposits that can reciprocate from side to side is incorporated in the gear groove of the 2-gear type coarse crushing and granulation device. 3. The dry granulation device according to claim 1, wherein a gear for removing deposits is incorporated in the groove of the vertically grooved roll of the roll granulator.
JP3791383A 1983-03-08 1983-03-08 Dry granulating apparatus Granted JPS59162937A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3791383A JPS59162937A (en) 1983-03-08 1983-03-08 Dry granulating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3791383A JPS59162937A (en) 1983-03-08 1983-03-08 Dry granulating apparatus

Publications (2)

Publication Number Publication Date
JPS59162937A JPS59162937A (en) 1984-09-13
JPS6365372B2 true JPS6365372B2 (en) 1988-12-15

Family

ID=12510782

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3791383A Granted JPS59162937A (en) 1983-03-08 1983-03-08 Dry granulating apparatus

Country Status (1)

Country Link
JP (1) JPS59162937A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103394307A (en) * 2013-07-25 2013-11-20 孙尚卫 Plant straw particle forming machine
CN107282182B (en) * 2017-07-06 2022-08-19 浙江物产汽车安全科技有限公司 Dry-process granulator
CN108272637B (en) * 2018-04-02 2021-08-20 青岛国海生物制药有限公司 Megestrol acetate dispersible tablet dry powder granulator

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5190354A (en) * 1975-02-07 1976-08-07 NETSUKOKASEIJUSHISEIKEIZAIRYONO SEIZOHO
JPS5559840A (en) * 1978-10-10 1980-05-06 Allis Chalmers Compactor

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5190354A (en) * 1975-02-07 1976-08-07 NETSUKOKASEIJUSHISEIKEIZAIRYONO SEIZOHO
JPS5559840A (en) * 1978-10-10 1980-05-06 Allis Chalmers Compactor

Also Published As

Publication number Publication date
JPS59162937A (en) 1984-09-13

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