JP5021129B2 - Compression molding equipment for bulky items - Google Patents
Compression molding equipment for bulky items Download PDFInfo
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- JP5021129B2 JP5021129B2 JP2001538062A JP2001538062A JP5021129B2 JP 5021129 B2 JP5021129 B2 JP 5021129B2 JP 2001538062 A JP2001538062 A JP 2001538062A JP 2001538062 A JP2001538062 A JP 2001538062A JP 5021129 B2 JP5021129 B2 JP 5021129B2
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- screw conveyor
- conveying direction
- compression molding
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- hopper
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B11/00—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
- B30B11/22—Extrusion presses; Dies therefor
- B30B11/24—Extrusion presses; Dies therefor using screws or worms
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/22—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic by pressing in moulds or between rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B11/00—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses
- B30B11/18—Presses specially adapted for forming shaped articles from material in particulate or plastic state, e.g. briquetting presses, tabletting presses using profiled rollers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B15/00—Details of, or accessories for, presses; Auxiliary measures in connection with pressing
- B30B15/30—Feeding material to presses
- B30B15/302—Feeding material in particulate or plastic state to moulding presses
- B30B15/308—Feeding material in particulate or plastic state to moulding presses in a continuous manner, e.g. for roller presses, screw extrusion presses
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Glanulating (AREA)
- Screw Conveyors (AREA)
- Processing Of Solid Wastes (AREA)
Description
【0001】
本発明は、ローラプレスと、かさのある品物(bulk goods)の供給装置としての供給ホッパを上方に取りつけ、そのローラプレスから上流側に配置されたスクリューコンベヤとを有しているかさのある品物用の圧縮装置に関する。
【0002】
粉体、粒状体又はそれらの混合体として供給される未加工製品(crude product )は、時としてさらなる次のプロセス例えば製薬産業における錠剤化に対し適切なものでない。なぜなら未加工製品は、空気の割合が非常に大きく及び/又は十分な流動性がないからである。さらなるプロセス及び続いてのそれらの造粒化の前に未加工製品を圧縮成形することは特許(独国特許第3431865号(German Patent 3431865 C2))において公知であるが、とりわけ実際的なものではない。例えば圧縮成形するためにスクリューコンベヤを有するローラプレスが、使用前に取りつけられる。スクリューコンベヤを使用して、未加工製品は供給ホッパからローラのギャップへ所定の圧力の下で供給される。
【0003】
ローラプレスが両側でシールされ、かつコンベヤがローラのギャップに気密的に接続されているので、圧縮時における未加工製品から追い出された空気は、スクリューハウジング内における原料を通って原料の運搬方向に対向して移動しなければならない。空気は続いて供給ホッパ内に配置された原料コラム介して流出してゆくかも知れないが、その原料コラムは高さと密度との関数において、空気に対して抵抗となる。しかしながら、空気の一部はローラのギャップを“爆発的”に通過してもゆくので、そのためにローラプレスは荷重を受けノズルを発生して運転される。
【0004】
圧縮成形にあたって、圧縮成形時に成形されるフレークは可能な限り均質であることがのぞましい。というのはこの特性が最終製品に対して直接的な影響を与えるからである。もし供給ホッパ内の未加工製品が、グレンサイズに関し又は他の特性に関して均一に分布していないと、不均質フレークが発生する。このことは、造粒化後に所定のグレンサイズを有していない圧縮成形された原料の一部が、供給ホッパへ再循環される場合特に発生する。この圧縮成形された未加工材料の直接的な再循環は問題がないわけではない。というのは、この圧縮成形された未加工製品のかさ比重と、未処理の未加工製品のかさ比重とが非常に違うからである。
【0005】
200g/lのかさ比重である未処理の未加工製品は、圧縮成形後の再循環原料として800g/lのかさ比重となるかも知れない。このことが再循環された製品の質量流量を大きく変動させている。柔らかなフレークにおいて、ローラプレスに供給される再循環された製品の質量流量の割合は大きく、このことは、フレークの均質な品質に好ましい影響を与えるけれど、再循環される原料の質量流量がそう失されるとの結果を招く。従って、フレーク品質の安定化はゆっくりとしたプロセスだけによりもたらされる。
【0006】
この理由により現在まで、再循環される原料の質量流量は、圧縮成形される前に未加工製品との補正的な混合過程を経ていた。
さらに、かさのある品物の圧縮成形装置が公知であって(独国特許出願公開第3806398A1( German Patent Application 3806398A1))、二つのシャフトを有している供給ホッパがローラプレスの上方に配置されていて、そのシャフトからローラギャップへ種々のタイプのかさのある品物が平行的に供給されてもよい。種々のシャフトからローラギャップへ供給される種々のタイプのかさのある品物の割合は、計量要素により調節されてもよい。ローラギャップを通過したかさのある品物は、粉砕され部分的に凝集化されすなわちフレークに圧縮される。一般にフレークは、最終処理のためにボールミルですり砕かれ、さらに移動装置へ供給され、その品質の劣った生産品が細粒製品として、細粒製品の供給装置を有しているシャフトへ再循環される。かさのある品物の脱気は、生産品であるかさのある品物用のシャフトにおける原料コラムを介して行なわれる。
【0007】
本発明の目的は、粒状化された製品及び造粒化された製品を圧縮成形するための装置を提供することであり、その装置は可能な限り均質に圧縮成形された製品を製造する。
【0008】
この目的は、本発明による以下に説明する圧縮成形装置により達成されている。
圧縮成形装置において:
供給ホッパが、スクリューコンベヤの運搬方向において前後して位置している少なくとも二つのシャフトを有していて、そのシャフトからスクリューコンベヤは、種々のタイプのかさのある品物を供給されかつ運搬方向において後段のシャフトにいたるまで下部から供給を受けており;
造粒物用分離装置を有する造粒化装置が、該ローラプレスの下流側へ接続され、造粒物をグレンサイズにより分離していて;
次のプロセスに適切でない造粒物の再循環が、運搬方向における分離装置から前段シャフトへ行なわれている。
【0009】
本発明における圧縮成形装置を使用することにより、均質なフレーク品質が全製造プロセスにわたって保証されている。この目的のために、未加工製品及びさらなる構成材料が種々のシャフトからスクリューコンベヤに当初から平行して供給されている。このことが、運搬方向において前段のシャフト(一つ以上)から構成材料の一部分だけをスクリューコンベヤに供給することを可能にし、一方未加工製品が後段シャフトからスクリューコンベヤに充填されることを可能にしている。分離装置により再循環された造粒物を含んでいる、スクリューコンベヤの運搬方向において行なわれるそれぞれの原料の供給により、圧縮成形されるべき原料の最適混合が、ミキサとして作用する多条スクリューコンベヤとの協働によりもたらされる。脱気に関して以下のことは好適なことであって、追い出された空気は後段シャフトにおける一般に充満している原料コラム全体を通過する必要はなく、むしろ、上流側シャフトの一つにおけるどちらにしても小さくて、一般に空である原料コラムだけを通過するだけでよい。
【0010】
次のプロセスに不適切であって再循環されるべき原料の割合は一般に僅かなものであって、この原料の入る供給ホッパのシャフトはどちらにしても部分的に充填されているだけで、大きな抵抗なしにこのシャフトを介しての脱気が可能である。
【0011】
好ましくは上流側の第一シャフトは、より大きなグレインを有する造粒物を供給されている。“より大きなグレイン”とは未加工製品に比較してより大きいグレインであることを意味している。この材料は、ねじの洗浄に適切なものであって、ローラプレスにおける供給を助ける役割も果していることが判明した。
以下に図面を参照して本発明を詳述する。
【0012】
圧縮成形装置は、未加工製品圧縮成形用部分1と、造粒化部分2と、造粒物分離部分3とで構成されている。
【0013】
第一部分1は、水平な材料供給装置を有するローラプレス4を含んでいる。圧縮成形される材料は、スクリューコンベヤ5を介して圧力下でローラプレス4のローラギャップに供給されていて、そのスクリューコンベヤ5は供給された材料を混合するためのスクリューハウジング5aと多条ねじ5bとを有している。スクリューコンベヤ5はローラギャップへ気密的に接続されている。
【0014】
ローラプレス4はカバープレート6により横方向でシールされている。前段シャフト7と後段シャフト9とに分割された、粒状化/造粒化された製品用の供給ホッパは、スクリューコンベヤ5の上方に配置されている。ロータ8は、未加工製品がシャフト7の中に滞留しないように移動するために、シャフト7の内部に取りつけられている。
【0015】
粒状化された未加工製品はシャフト7へ導入される。スクリューコンベヤ5が、その未加工製品をローラプレス4のローラギャップに圧力下で供給していて、そこでその未加工製品はフレークSに圧縮成形される。フレークSは続いて装置の部分2において造粒化される。造粒物Gは通常巾広の粒状パレットであることから、それ以降のプロセスに適切なものではない。従って、装置における連続した部分3において、その粒状パレットは、以降のプロセスに適切な造粒物G1と、供給ホッパのシャフト9へ再循環される造粒物G2とに分離される。造粒物G2の質量流量が少ないので、スクリューコンベヤ5は部分的にそれを供給されるだけである。供給の残りはシャフト7における未加工原料である。従って、生産プロセスの初期段階においてさえも、スクリューコンベヤはシャフト7,9の両方から種々の特性の材料を平行して供給される。このことが、所望される均質なフレーク品質に対してポジティブな作用を行なっている。
【図面の簡単な説明】
【図1】 図1は圧縮成形装置の部分概略図である。[0001]
The present invention relates to a bulky article having a roller press and a screw conveyor disposed on the upstream side of the roller press with a feeding hopper as a bulk goods feeding device mounted thereon. The present invention relates to a compression apparatus for use.
[0002]
Crude products supplied as powders, granules or mixtures thereof are sometimes not suitable for further subsequent processes such as tableting in the pharmaceutical industry. This is because the raw product has a very high proportion of air and / or lacks sufficient fluidity. It is known in the patent (German Patent 3431865 C2) to compress the green products before further processing and subsequent granulation of them, but in particular practically Absent. For example, a roller press with a screw conveyor for compression molding is installed before use. Using a screw conveyor, the raw product is fed from the feed hopper into the roller gap under a certain pressure.
[0003]
Since the roller press is sealed on both sides and the conveyor is hermetically connected to the roller gap, the air expelled from the raw product during compression will pass through the raw material in the screw housing in the direction of raw material transport. Must move in opposition. Although air may subsequently flow out through a raw material column located in the supply hopper, the raw material column is resistant to air as a function of height and density. However, some of the air can “explosively” pass through the roller gap, so the roller press is operated under load and generating nozzles.
[0004]
In compression molding, the flakes formed during compression molding should be as homogeneous as possible. This is because this property has a direct impact on the final product. If the raw product in the feed hopper is not evenly distributed with respect to grain size or other characteristics, heterogeneous flakes will occur. This occurs particularly when a portion of the compression-molded raw material that does not have a predetermined grain size after granulation is recycled to the supply hopper. This direct recycle of the compression molded raw material is not without problems. This is because the bulk specific gravity of this compression molded raw product is very different from the bulk specific gravity of the unprocessed raw product.
[0005]
An untreated raw product with a bulk specific gravity of 200 g / l may have a bulk specific gravity of 800 g / l as a recycled material after compression molding. This greatly fluctuates the mass flow rate of the recycled product. In soft flakes, the proportion of the mass flow rate of the recycled product fed to the roller press is large, which has a positive effect on the homogeneous quality of the flakes, but the mass flow rate of the recycled material does not. Results in being lost. Therefore, stabilization of flake quality is only brought about by a slow process.
[0006]
For this reason, to date, the mass flow rate of the recycled material has undergone a corrective mixing process with the raw product before compression molding.
Further, a compression molding apparatus for bulky products is known (German Patent Application Publication No. 3806398A1 ( German Patent Application 3806398 A1)), a supply hopper having two shafts may be arranged above the roller press, and various types of bulk goods may be supplied in parallel from the shaft to the roller gap. The proportion of different types of bulky items fed from different shafts to the roller gap may be adjusted by a metering element. The bulky product that has passed through the roller gap is crushed and partially agglomerated, ie compressed into flakes. In general, flakes are ground in a ball mill for final processing, and further fed to a moving device. The inferior product is recirculated as a fine-grained product to a shaft that has a fine-grained product feeder. Is done. The degassing of the bulky item is performed via a raw material column in the shaft for the bulky product that is the product.
[0007]
It is an object of the present invention to provide an apparatus for compression molding granulated products and granulated products, which produces a compression molded product as homogeneously as possible.
[0008]
This object is achieved by the compression molding apparatus described below according to the present invention.
In compression molding equipment:
The supply hopper has at least two shafts that are located back and forth in the conveying direction of the screw conveyor, from which the screw conveyor is fed with various types of bulky items and is downstream in the conveying direction. From the bottom to the end of the shaft;
A granulating device having a granulating material separating device is connected to the downstream side of the roller press and separates the granulated material by the grain size;
Recirculation of the granulate which is not suitable for the next process takes place from the separating device in the conveying direction to the front shaft.
[0009]
By using the compression molding apparatus in the present invention, homogeneous flake quality is assured throughout the entire manufacturing process. For this purpose, raw products and further components are supplied from the various shafts in parallel to the screw conveyor from the beginning. This makes it possible to feed only a part of the constituent material from the front shaft (one or more) to the screw conveyor in the conveying direction, while allowing raw products to be filled from the rear shaft into the screw conveyor. ing. A multi-threaded screw conveyor that contains the granulated material recirculated by the separator, and that provides the optimum mixing of the raw material to be compression-molded by feeding each raw material in the conveying direction of the screw conveyor. Brought about by collaboration. With regard to deaeration, the following is preferred and the expelled air does not have to pass through the generally full feed column in the back shaft, but rather in either of the upstream shafts. It only needs to pass through a small, generally empty, raw material column.
[0010]
The proportion of raw material that is unsuitable for the next process and has to be recycled is generally small and the feed hopper shaft containing this raw material is only partially filled anyway, Deaeration through this shaft is possible without resistance.
[0011]
Preferably, the upstream first shaft is supplied with a granulated product having larger grains. “Bigger grain” means larger grain compared to the raw product. It has been found that this material is suitable for screw cleaning and also plays a role in assisting feeding in roller presses.
The present invention will be described in detail below with reference to the drawings.
[0012]
The compression molding apparatus is composed of a raw product compression molding part 1, a granulated part 2, and a granulated product separating part 3.
[0013]
The first part 1 includes a roller press 4 having a horizontal material supply device. The material to be compression-molded is supplied to the roller gap of the roller press 4 under pressure through the screw conveyor 5, and the screw conveyor 5 mixes the supplied material with a screw housing 5a and a multi-thread screw 5b. And have. The screw conveyor 5 is hermetically connected to the roller gap.
[0014]
The roller press 4 is sealed laterally by a cover plate 6. A supply hopper for granulated / granulated products divided into a front shaft 7 and a rear shaft 9 is arranged above the screw conveyor 5. The rotor 8 is attached to the inside of the shaft 7 so that the raw product moves so as not to stay in the shaft 7.
[0015]
The granulated raw product is introduced into the shaft 7. A screw conveyor 5 feeds the raw product into the roller gap of the roller press 4 under pressure, where the raw product is compression molded into flakes S. The flakes S are subsequently granulated in part 2 of the device. Since the granulated product G is usually a wide granular pallet, it is not suitable for the subsequent processes. Thus, in a continuous part 3 of the apparatus, the granular pallet is separated into a granulation G1 suitable for the subsequent process and a granulation G2 which is recycled to the shaft 9 of the feed hopper. Since the mass flow rate of the granulated product G2 is small, the screw conveyor 5 is only partially supplied with it. The remainder of the supply is raw material in the shaft 7. Thus, even in the early stages of the production process, the screw conveyor is fed in parallel with materials of various properties from both shafts 7,9. This has a positive effect on the desired homogeneous flake quality.
[Brief description of the drawings]
FIG. 1 is a partial schematic view of a compression molding apparatus.
Claims (3)
該供給ホッパが、該スクリューコンベヤ(5)の運搬方向において前後して配置されている少なくとも二つの供給ホッパ(7,9)を有していて、その供給ホッパ(7,9)から該スクリューコンベヤ(5)は、種々のタイプのかさのある品物を供給されかつ運搬方向において後段の供給ホッパ(7)にいたるまで供給ホッパの下部から併行して供給を受けており、従って供給ホッパ(7,9)から該スクリューコンベヤ(5)の運搬方向にそれぞれ別の材料が併行して供給されていて、未加工製品は該運搬方向において該後段のホッパ(7)から該スクリューコンベヤ(5)に供給されていて、
造粒物(G)用分離装置(3)を有する造粒化装置(2)が、該ローラプレス(4)の下流側へ接続され、該造粒物(G)をグレインサイズにより分離しており、そして該造粒化装置が再循環ガイドを有していて、該再循環ガイドは、該分離装置(3)と該運搬方向において前段の供給ホッパ(9)とを接続していて、次のプロセスに適切でない造粒物(G2)を該運搬方向において前段の供給ホッパ(9)へ再循環していて、再循環された該造粒物(G2)は該運搬方向において前段の供給ホッパ(9)から該スクリューコンベヤ(5)に供給されていること、
を特徴としている圧縮成形装置。A roller press (4), and a screw conveyor (5) disposed upstream from the roller press (4) and having a supply hopper as a supply device for a bulky article disposed above, In compression molding equipment for bulky items:
The supply hopper has at least two supply hoppers (7, 9) arranged back and forth in the conveying direction of the screw conveyor (5), from the supply hopper (7, 9) to the screw conveyor In (5), various types of bulk goods are supplied and supplied in parallel from the lower part of the supply hopper to the subsequent supply hopper (7) in the conveying direction . 9) to the screw conveyor (5) in the conveying direction, different materials are supplied in parallel, and raw products are supplied in the conveying direction from the subsequent hopper (7) to the screw conveyor (5). Have been
A granulating device (2) having a separating device (3) for the granulated product (G) is connected to the downstream side of the roller press (4), and separates the granulated product (G) by grain size. And the granulation device has a recirculation guide, which connects the separation device (3) and the feed hopper (9) in the preceding stage in the conveying direction, The granulated product (G2) that is not suitable for the above process is recycled in the conveying direction to the preceding feed hopper (9), and the recycled granulated product (G2) is recycled in the conveying direction to the preceding feed hopper. Being supplied to the screw conveyor (5) from (9),
A compression molding device characterized by
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19955484.6 | 1999-11-17 | ||
DE19955484 | 1999-11-17 | ||
DE10007731A DE10007731B4 (en) | 1999-11-17 | 2000-02-19 | Compacting plant for bulk materials |
DE10007731.5 | 2000-02-19 | ||
PCT/EP2000/011368 WO2001036079A1 (en) | 1999-11-17 | 2000-11-16 | Compacting system for bulk material |
Publications (2)
Publication Number | Publication Date |
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JP2003515452A JP2003515452A (en) | 2003-05-07 |
JP5021129B2 true JP5021129B2 (en) | 2012-09-05 |
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Application Number | Title | Priority Date | Filing Date |
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JP2001538062A Expired - Lifetime JP5021129B2 (en) | 1999-11-17 | 2000-11-16 | Compression molding equipment for bulky items |
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JP (1) | JP5021129B2 (en) |
DE (2) | DE10007731B4 (en) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5559840A (en) * | 1978-10-10 | 1980-05-06 | Allis Chalmers | Compactor |
US4439384A (en) * | 1981-12-16 | 1984-03-27 | Maschinenfabrick Koppern Gmbh & Co. Kg | Method for manufacturing graules from potassium chloride fines |
JPS6018424Y2 (en) * | 1979-09-19 | 1985-06-04 | バブコツク日立株式会社 | Coal slurry production equipment |
DE3806398A1 (en) * | 1988-02-29 | 1989-09-07 | Kloeckner Humboldt Deutz Ag | Two-roller machine for pressure treatment of granular material and method for operating such a machine |
JPH04176372A (en) * | 1990-11-09 | 1992-06-24 | Nippon Steel Corp | Fine powder separator for fine powder lumping machine |
US5184779A (en) * | 1990-09-14 | 1993-02-09 | Degussa Akiengesellscahft | Method of producing granulated material composed of zinc oxide and silica, resulting product and its use |
JPH06297197A (en) * | 1993-04-14 | 1994-10-25 | Nippon Steel Corp | Method and device for dry granulation |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
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DE1778089A1 (en) * | 1968-03-28 | 1971-09-30 | Alexanderwerk Ag | Granulating press |
DE1807714C2 (en) * | 1968-11-08 | 1971-01-04 | Degussa | Process and device for continuous pre-compression and simultaneous shaping of finely divided materials |
DE2151310C2 (en) * | 1971-10-15 | 1973-12-06 | Erich August 4034 Angermund Hindermann | Dosing, mixing and conveying device |
US4467969A (en) * | 1979-05-23 | 1984-08-28 | Standard Oil Company | On-line reclaim system |
DE3431865A1 (en) * | 1984-08-30 | 1986-03-06 | Degussa Ag, 6000 Frankfurt | METHOD AND DEVICE FOR GRANULATING POWDERED SUBSTANCES |
JPH04499A (en) * | 1990-04-13 | 1992-01-06 | Roland Corp | Electronic musical instrument |
-
2000
- 2000-02-19 DE DE10007731A patent/DE10007731B4/en not_active Expired - Fee Related
- 2000-11-16 JP JP2001538062A patent/JP5021129B2/en not_active Expired - Lifetime
- 2000-11-16 DE DE50003037T patent/DE50003037D1/en not_active Expired - Fee Related
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5559840A (en) * | 1978-10-10 | 1980-05-06 | Allis Chalmers | Compactor |
JPS6018424Y2 (en) * | 1979-09-19 | 1985-06-04 | バブコツク日立株式会社 | Coal slurry production equipment |
US4439384A (en) * | 1981-12-16 | 1984-03-27 | Maschinenfabrick Koppern Gmbh & Co. Kg | Method for manufacturing graules from potassium chloride fines |
DE3806398A1 (en) * | 1988-02-29 | 1989-09-07 | Kloeckner Humboldt Deutz Ag | Two-roller machine for pressure treatment of granular material and method for operating such a machine |
US5184779A (en) * | 1990-09-14 | 1993-02-09 | Degussa Akiengesellscahft | Method of producing granulated material composed of zinc oxide and silica, resulting product and its use |
JPH04176372A (en) * | 1990-11-09 | 1992-06-24 | Nippon Steel Corp | Fine powder separator for fine powder lumping machine |
JPH06297197A (en) * | 1993-04-14 | 1994-10-25 | Nippon Steel Corp | Method and device for dry granulation |
Also Published As
Publication number | Publication date |
---|---|
DE10007731A1 (en) | 2001-06-13 |
DE10007731B4 (en) | 2005-12-01 |
JP2003515452A (en) | 2003-05-07 |
DE50003037D1 (en) | 2003-08-28 |
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