子分类：
- B01J2/003： .{后续颗粒涂覆}(阻止颗粒粘结聚集入B01J 2/30)
- B01J2/006： .{涂覆颗粒,但是没有描述方法或所用设备}(预防颗粒粘结聚集入B01J 2/30)
- B01J2/02： .将液体原料分成珠滴,例如喷雾和固化成珠(喷雾蒸发入B01D 1/16)
- B01J2/10： .在装备有搅拌或混合装置的静置罐或槽内
- B01J2/12： .在旋转罐内
- B01J2/14： .在旋转盘或锅内
- B01J2/16： .将粉末原料悬浮在一种气体中,例如在流化床内或像一个向下流动的帘幕内
- B01J2/18： .用一振动装置
- B01J2/20： .将原料挤压,例如,通过网眼并切断挤出的长条
- B01J2/22： .在模子内或在两辊子间挤压
- B01J2/24： .从一表面刮掉固体层而获得片状粉末
- B01J2/26： .在环形传送带上
- B01J2/28： .使用特殊的黏合剂
- B01J2/30： .使用附加剂防止颗粒黏结在一起;使颗粒物质成为自由流动材料,例如使它们成为憎水的
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 241 | Method of manufacturing a weakly agglomerated nano scalar particle | JP53298396 | 1996-04-26 | JP4129564B2 | 2008-08-06 | ヘルムート シュミット; リューディガー ナス; デートレフ ブルガード |
| 242 | Method and apparatus for producing inorganic spheres particles | JP22800297 | 1997-08-25 | JP3501631B2 | 2004-03-02 | 徳久 中島; 晃 小林; 晋 水谷 |
| 243 | Fluidization bisphenol dust | JP2001549326 | 2000-12-11 | JP2003519107A | 2003-06-17 | ニコライ・コステュスツュン; フリーダー・ヘイデンライヒ; ミヒャエル・プライン; ミヒャエル・ベーディガー; ライナー・ノイマン; ロルフ・ランツェ |
| (57)【要約】 本発明は、ビスフェノール・ダストおよび水からなる流動化ビスフェノールダスト、その製造方法およびビスフェノールダストを製造工程に加えるビスフェノールの製造方法に関する。 | ||||||
| 244 | Apparatus and method for granulating the powdery material | JP17611890 | 1990-07-03 | JP3284218B2 | 2002-05-20 | スベンド、ダニエルセン; トルベン、シェファー; ヘニング、グジェルストルプ、クリステンセン; ペル、ホルム |
| 245 | Colloidal particles, as well as methods for their preparation of the solid flame retardant and smoke suppressant | JP50219997 | 1996-06-07 | JP2000516269A | 2000-12-05 | ジョン・アール・マックローグリン; ジョン・シー・モレー; フィリップ・エス・ポドウィアニー |
| (57)【要約】 本発明は、繊維、織物、ポリマー製物品、紙、塗料、コーティング、および絶縁材料に対して、難燃性および／または煙抑制性を提供する化合物の微細に分割された粒子に関する。 より特定すると、本発明は、含水塩、有機ホスフェート、金属ボレート、ポリアミド、250℃を上回る融点を有する固体ハロゲン化難燃剤、モリブデン化合物、メタロセン、アンチモン化合物、亜鉛化合物、ビスマス化合物、および難燃剤または煙抑制剤として作用する他の固体化学種のコロイドサイズの粒子に関する。 本発明はまた種々の粉砕プロセスに関し、これらの材料をコロイドサイズにまで小さくし、そしてそれらを水、有機液体、および溶融性の固体中に分散させる。 | ||||||
| 246 | Granular detergent / cleaning agents or production methods of its components | JP52480097 | 1996-12-20 | JP2000503055A | 2000-03-14 | エンゲルス，ヘンリッヒ; マルシュナー，ミヒャエル |
| (57)【要約】 本発明は、粒状洗剤／洗浄剤またはその成分を、粒状化剤を用いてミキサーによって製造する方法であって、上記粒状化剤は、粒状化される成分の少なくとも一部に対し系内で液体形態の水に変化しうる水蒸気であり、その水分吸収量は、粒状化される成分に対し 0.1〜2 重量％であることを特徴とする方法を提供する。 この方法は、特に微粉砕した成分から、その後の乾燥処理を必要とせずに粒状化剤として作用する「水蒸気」によって粒状材料を形成する。 | ||||||
| 247 | Material granulate for frictional material and manufacture thereof | JP30203297 | 1997-11-04 | JPH11129252A | 1999-05-18 | SUKAI YUKIYASU |
| PROBLEM TO BE SOLVED: To easily manufacture at low cost material granulate for frictional material without requiring a special device by a method wherein primary granulate which are formed by granulating a starting material containing the fibrous material of the frictional material, a powder material and a binder, are crushed. SOLUTION: In order to produce material granulate for frictional material (or secondary granulate) suitable for the manufacturing of the frictional material used in the brake, clutch or the like of various vehicles, industrial equipments or the like, first of all, primary granulated matters are produced. Concretely, a fibrous material, a powder material and a binder, which are metered so a to form a predetermined mixing ratio, are charged in a mixing device so as to uniformly mix these materials in order to obtain a starting material. Next, by adding the proper amount of water to the mixing device and then rolling the starting material, a primary granulate 1 is obtained. After that, by crushing the primary granulate 1 in the same mixing device, the secondary granulate 2 are obtained. The crushing is performed by a method, in which a rolling speed (or the rotating speed of the rotating blade of the device) is made faster than that at the granulating time of the primary granulate 1 is made higher in order to collide the primary granulate with one another, or the like. COPYRIGHT: (C)1999,JPO | ||||||
| 248 | Nano-scale particles and their use | JP50886996 | 1995-08-25 | JPH10505538A | 1998-06-02 | ターチャン，マニュエル，シー; ミストリィ，プラビン; リウ，シェングズホング |
| (57)【要約】 ナノスケール粒子及び粉末は、大きなサイズのスタート粒子及び固体ターゲットを含むスターティング原料から作られる。 レーザーと電気アークと火炎とプラズマとから構成されるグループから選択されるエネルギー源でスターティング原料を加熱と分解することを全てほぼ含む様々な技術が開示されている。 ここに開示される様々な技術はすべて、高いスループットと、多様な応用の為のナノスケール粉末のほぼ瞬間的な製造速度とを示している。 実施例のある物において、ナノスケール粒子の大きい（非ナノスケール）粒子への塊状集積を防止するために冷却が必要とされる。 ナノスケール粒子は、ペイント、コーティング、結合、接合、ハンダ付け、ロウ付け、溶接等に有用である。 例えば、結合（例えば、ロウ付け）に通常伴う熱応力は、本発明の低温結合技術により、低減され得る。 低温結合材料は、（ペーストとして、或いは粉末スプレーとして、或いはテープとして、或いはペイントとして、或いはパテとして）共に結合されることが望まれる二つの要素の結合部に供給される。 レーザー光線（例えば、Ｎｄ：ＹＡＧ或いは二酸化炭素レーザー）のような源からの、或いは火炎、アーク、プラズマ等によるエネルギーが、結合材料に沿って移動され結合材料の全部を反応させるか、結合材料が自律反応型であり且つ単純にエネルギー源による結合材料の選択された部分の点火を必要とするかである。 工程の模範的適用において、好適には低温結合材料を使用して、翼はボール及び／又は自動変速機ボール（インペラー或いはタービン）組立体のシュラウドにロウ付けされる。 結合材料とエネルギーを供給するシステムが記載される。 窪み翼の製作が記載される。 シュラウドボール要素の製造と、シュラウドの機能を包含するステーター要素とが記載される。 | ||||||
| 249 | Production of particulate neopentyl glycol hydroxypivalate, particle produced thereby and granulation of the particle with granulator | JP24895597 | 1997-09-12 | JPH10114709A | 1998-05-06 | WEYER HANS-JUERGEN DR; ECK BERND; BAUMANN DIETER; MALTRY BERNHARD |
| PROBLEM TO BE SOLVED: To provide a process for producing particles of neopentyl hydroxypivalate(NHP) free from the defects of conventional process while suppressing the generation of cake, provide a particulate NHP having low cake-generation rate and provide a process for granulating the particle with a granulator. SOLUTION: This process for the production of particulate NHP comprises the supply of a molten NHP containing >=3wt.% of NHP crystal based on the total weight of NHP to a cooling zone to solidify the molten NHP. A particulate NHP having low caking tendency can be produced by this process. The particles can be granulated by a method using a granulator for molten material provided with a precooling device 2, a precrystallizer 3, a liquid droplet forming machine 4 or a planar applicator, a cooling belt 6 and a crusher in the case of using a planar applicator. | ||||||
| 250 | Continuously granulating apparatus to prepare granule and continuous granulation | JP28375796 | 1996-10-25 | JPH09173037A | 1997-07-08 | FUKAZAWA MASAHIRO; YOSHIOKA KAZUO; YOSHIZAWA SHOICHI |
| PROBLEM TO BE SOLVED: To provide an apparatus for continuously granulating a porous granule excellent in instant solubility. SOLUTION: This apparatus is equipped with a feeding means 8 for continuously supplying a powdery raw material, a granulating zone 14 for granulating the supplied raw material powdery and a drying zone 16 for drying the granule, a granulating tank 2 formed into a bathtub shape, a spray nozzle 30 for adding a binder to the powdery raw material, a flat perforated plate 20 arranged at the lower part of the granulating zone 14 and the drying zone 16, a laminar intermediate weir 15 laid approximately in the vertical direction between the granulating zone 14 and the drying zone 16 of the granulating tank to form spaces, an outlet weir 17 which is installed at the outlet side of the drying zone 16 and overflows the granulated powdery raw material and heated air supplying means 24 and 26 for blowing up the heated air from the bottom of the flat perforated plate 20 to the granulating zone 14 and the drying zone 16 and forming a fluidized bed. | ||||||
| 251 | Spherical granule of water-soluble azo compound and method for producing the same | JP4770994 | 1994-02-21 | JPH07233133A | 1995-09-05 | AMOU HIDEO; KAGOMOTO SEIYA; GOTO AKIHIKO |
| PURPOSE: To provide a method for producing the spherical granules of a water-soluble azo compound, capable of safely obtaining the spherical water-soluble azo compound substantially not generating dust. CONSTITUTION: A method for producing the spherical granules of a water-soluble azo compound comprises dispersing a water-soluble azo compound in 1-100 times weight, preferably 1.5-20 times weight of a water-insoluble solvent, dropping a hydrophilic solvent capable of dissolving the water-soluble azo compound in an amount capable of partially dissolving the water-soluble azo compound (preferably in an amount of 3-20wt.% based on the water-soluble azo compound) for granulating the dispersed water-soluble azo compound in the solution, filtering the obtained spherical granule suspension for separating only the spherical granules, and subsequently drying the separated granules. The method can especially be applied to an azo compound of formula I [R 1, R 2 are alkyl, cycloalkyl; Z is a group of formula II or III (R 3 is H, alkyl, allyl, phenyl which can be substituted; R 4 is R 3 excluding allyl; R 5 is alkylene which can be substituted; R 6 is H, hydroxyalkyl; X is Cl, Br, CH 3COO)] or a group of formula IV [A is alkylene which can be substituted; R 7 is alkyl; Y is alkali metal, alkaline earth metal (2Y), NH 4]. COPYRIGHT: (C)1995,JPO | ||||||
| 252 | Photographing apparatus in granulation, coating, and the like | JP28883393 | 1993-10-26 | JPH07120374A | 1995-05-12 | WATANO SATORU; ITO YOSHIHIRO; ODA NOBUTO; KAMATA TETSUO; KAWAKAMI NOBORU; MORIYA SHINJI |
| PURPOSE: To obtain the clear images of particles which are separated completely from each other by a method wherein air is supplied respectively from an air supply port to a photographing system and from a slit of an illumination system, the adhesion of the particles is prevented, the particles are dispersed by longitudinal and transverse air streams and the particles are photographed. CONSTITUTION: The tip part 41 of a photographing apparatus in which both and illumination system 45 and a photographing system have been installed is arranged near particles which are being granulated inside a tank. The tip of the illumination system 45 is extended further than the tip of the photographing system, a slit 47 which is directed in the direction at a right angle to the shaft is formed, and an optical-fiber bundle 46 which is connected to a high-speed electronic flash light-emitting source is arranged. When air is supplied from air supply ports 51, 52, the air is passed respectively through a gap 44 for the photographing system and a gap 49 around the optical-fiber bundle 46, one part is jetted in the direction of the axial line of the photographing system, and the other part is jetted in the direction perpendicular to the axial direction through the slit 47. Many particles which have been clustered together near the tip part 41 are separated from the tip part by the two air streams, and the remaining particles are separated individually by the air stream from the slit 47. In this state, an electronic flash is turned on, the particles are photographed, and the clear image of the particles is obtained. COPYRIGHT: (C)1995,JPO | ||||||
| 253 | JPH06507571A - | JP50333292 | 1991-12-18 | JPH06507571A | 1994-09-01 | |
| 254 | JPH0566172B2 - | JP10806085 | 1985-05-20 | JPH0566172B2 | 1993-09-21 | HANSU RAUENBERUGAA |
| 255 | Process and apparatus for purifying chemical substance | JP36112191 | 1991-12-18 | JPH04300602A | 1992-10-23 | KONRATSUDO SHIERUMUTSUKII; HERUBERUTO BUYURUMUZEAA |
| PURPOSE: To continuously and economically purify a chemical substance by making a molten chemical substance drop-shape, deheating, crystallizing and solidifying the droplets to form pellets, subjecting the pellets to a sweating process by a hot gas flow to melt outer contaminated surfaces of the pellets and to drip off the melt to attain purification of the pellet. CONSTITUTION: A molten chemical substance is made to be drop-shaped at first, is deheated, then is crystallized and solidified to form pellets 8. Then the pellets 8 are supplied to a perforated incline bottom surface 17 of a vessel 10 from a feeding conduit 9, the pellets 8 are subjected to the sweating process by the hot gas flow 21 to melt the outer contaminated surfaces thereof and to drip off the melt 22 to attain purification of the pellet 8 and purified pellets 8' are taken out from a carrier shoot 12. Consequently the chemical substance can be continuously and economically purified. COPYRIGHT: (C)1992,JPO | ||||||
| 256 | JPH04502423A - | JP51155489 | 1989-10-12 | JPH04502423A | 1992-05-07 | |
| 257 | Paateikyureetohatsuseisochi | JP11644382 | 1982-07-03 | JPH0236180B2 | 1990-08-15 | ISHIDA KOZO; OKAYAMA JUNJI; OOTSUKI KUNIO |
| 258 | JPH01501768A - | JP50192687 | 1987-03-04 | JPH01501768A | 1989-06-22 | |
| 259 | JPS6036839B2 - | JP6179175 | 1975-05-23 | JPS6036839B2 | 1985-08-22 | JEEMUSU EMU OODONNERU |
| 260 | JPS5710141B2 - | JP10887773 | 1973-09-27 | JPS5710141B2 | 1982-02-25 | |
| Pelleted sulfur compositions consisting essentially of particles of sulfur which include a substantial proportion of carbon-disulfide-insoluble sulfur particles together with a binder consisting essentially of a plasticizing or softening oil containing an anionic or nonionic surfactant in an amount equivalent to between 0.5 and 10% of the weight of the pelleted composition, the pelleted composition containing an amount of the plasticizing oil equivalent to between 10 and 60% of its weight. The pelleted composition is free-flowing, storable, and disperses homogeneously when distributed in rubber mixtures by milling on heated compounding rolls. | ||||||
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