| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 81 | 制备粒状材料的方法 | CN94194131.0 | 1994-11-12 | CN1082828C | 2002-04-17 | 杰哈德·盖尔盖伊; W·特里哈特 |
| 为了从至少含有两种组份，其中一种是晶体或结晶型的，并且至少有一种是含有结晶水的和/或具有反应活性的组份的混合物粉末制粒，在一个倾斜的鼓(5)的一端加进粉末进行粒化，在另一端取出粒化材料。粉末加入鼓(5)中之后，在给定的时间内进行反应，在此期间，物料不断滚动以尽量避免由剪切力强迫进行输送。同时在鼓中应提供至少接近物料中存在的结晶水的液体量以生成将表面粘合的粘液。使粉末混合物组份通过表面粘着而粒化。在给定情况下也可通过具有反应活性的组分的部分反应而生成这种液体。 | ||||||
| 82 | 球状含药细粒的制备方法 | CN99815061.4 | 1999-10-22 | CN1331583A | 2002-01-16 | 石桥隆; 永尾惠吾; 池上谦吾; 吉野广祐; 沟边雅一 |
| 本发明公开一种可供生产易吞服控释制剂的球状含药细粒的有效制备方法,此方法的特征在于将粘合剂溶液加入到含有溶剂保留赋形剂粉末(优选其长轴的平均直径为40微米或更小)和药物粉末(优选其长轴的平均直径为50微米或更小)的混合物中,高速旋转造粒制得球状含药细粒(平均粒度为60－200微米)。 | ||||||
| 83 | 致密洗涤剂组合物的制备方法 | CN93109037.7 | 1993-06-15 | CN1045988C | 1999-10-27 | P·范迪克; J·L·韦加 |
| 用于连续制备体积密度高于650g/l的粒状洗涤剂组合物或组分的方法，该方法包括如下步骤：i)在停留时间为2秒-30秒的高速混合器中，将洗涤剂活性浆体完全分散于粉末流中，ii)在停留时间少于2分钟的中速混合器/团聚机中形成附聚物，其中，也可任意加入精细粉碎粉末。iii)干燥和/或冷却。用此方法制得的粒状洗涤剂组合物，其具有出色的溶解性能，还特别地就分配和溶解速率进行了描述。 | ||||||
| 84 | 制备粒状材料的方法 | CN94194131.0 | 1994-11-12 | CN1135189A | 1996-11-06 | 杰哈德·盖尔盖伊; W·特里哈特 |
| 为了从至少含有两种组分，其中一种是晶体或结晶型的，并且至少有一种是含有结晶水的和/或具有反应活性的组分的混合物粉末制粒，在一个倾斜的鼓(5)的一端加进粉末进行粒化，在另一端取出粒化材料。粉末加入鼓(5)中之后，在给定的时间内进行反应，在此期间，物料不断滚动以尽量避免由剪切力强迫进行输送。同时在鼓中应提供至少接近物料中存在的结晶水的液体量以生成将表面粘合的粘液。使粉末混合物组分通过表面粘着而粒化。在给定情况下也可通过具有反应活性的组分的部分反应而生成这种液体。 | ||||||
| 85 | 离心筛制粒机 | CN200820082409.2 | 2008-01-17 | CN201105216Y | 2008-08-27 | 范春雷; 寿旭锋; 曲建全 |
| 本实用新型是一种在医药和生化领域内制备颗粒用的离心筛制粒机。现有颗粒制备多采用乳化或滴液方式，生产设备复杂易堵塞、生产效率低只能批次间断加料进行，制备的颗粒大小各异，一致性差，乳化制备的颗粒内部残存有矿物油严重影响颗粒质量。本实用新型提供了一种能够在无污染的封闭环境下连续高效制备颗粒的离心筛制粒机，包括一个反应罐，其上部接有进液管，底部接有收集管，罐内设有一个可更换的侧壁开有复数个筛孔的筛桶，反应罐顶部设有一个和筛桶连通的加料管，筛桶安装在转轴上，转轴穿过反应罐和外置调速电机连接。本实用新型利用离心力甩出生产原液和另一原液结合反应连续高效的制备颗粒，更换筛桶和改变筛桶转速还能调整颗粒粒径。 | ||||||
| 86 | Continuous reaction apparatus and apparatus for producing a toner | US15368034 | 2016-12-02 | US09983492B2 | 2018-05-29 | Yuqing Xu |
| Provided is a continuous reaction apparatus which can precisely control the path of flow of the liquid reaction mixture in the reaction vessel. Further, provided is a continuous reaction apparatus which can efficiently mix the liquid reaction mixture in the reaction vessel. The continuous reaction apparatus comprises a plurality of mixing vessel units and a plurality of partition units. These units are connected in the state of being alternately stacked on one another. Each mixing vessel unit has an agitating blade disposed in the inner space thereof. The relationship between the inner diameter D1 of the mixing vessel unit, the height H of the mixing vessel unit, and the outer diameter d1 of the agitating blade satisfies the formula (1): 10≥(D1/H)≥1.5, and the formula (2): 0.99≥(d1/D1)≥0.7. The agitating blade is a circular disc-type agitating blade. | ||||||
| 87 | GRANULATED BODY MANUFACTURING APPARATUS AND METHOD | US15365306 | 2016-11-30 | US20170157642A1 | 2017-06-08 | Takeyuki OZAKI; Yasuhiro SAKASHITA; Takenori IKEDA |
| A granulated body manufacturing apparatus includes: a housing that includes a cylindrical internal space, is disposed so that a center axis direction of the internal space is horizontal, and houses a raw material for a granulated body inside the internal space; an agitation blade that is provided along an inner circumferential surface of the internal space, and upon being rotated around the center axis, scoops up the raw material accumulated in a bottom portion of the internal space and makes the raw material fall down from an upper position inside the internal space; and a crossing blade including a wire having a wire diameter not exceeding 0.3 mm, the wire being provided at a position in a range, inside the internal space, in which the crossing blade does not come into contact with the agitation blade, and being looped around a framework body that rotates around the center axis. | ||||||
| 88 | Solid aggregates of microparticles, system and method for producing such aggregates | US15359863 | 2016-11-23 | US20170144123A1 | 2017-05-25 | Patrick Tabeling; Joshua Ricouvier; Bingqing Shen |
| The present invention lies within the field of colloidal assemblies and relates to a system for producing solid clusters of microparticles, characterized in that it comprises at least: a fluidic device comprising at least: an element for producing primary droplets, comprising an outlet of width l1 and a main channel for forming solid clusters, having a main axis, of height h2 and comprising an inlet of width l2; said element for producing primary droplets being connected to said inlet of said main channel, h1 being less than h2, so as to form a step between said element for producing primary droplets and said main channel and l1 being strictly less than l2; a system of physical initiation of polymerization capable of initiating polymerization in said main channel. | ||||||
| 89 | Device and method for producing polymer agglomerates | US13990544 | 2011-03-03 | US09440374B2 | 2016-09-13 | Raimund Schwarz; Stephan Poller; Markus Brunkau; Thomas Schill; Dick Van Dijk |
| The invention relates to a device (1) for producing polymer agglomerates, comprising a compounder (2) having a housing (21) and a twin screw (22) arranged therein as well as a plurality of material inlets (3, 4) for admission of a polymer and additives, tempering units for heating the mix comprising polymer and additives, at least one degassing unit (5) and an outlet (23) and an agglomerating vessel (11) having an agglomerating tool (8) and a cooling tool (10). The agglomerating vessel (11) is connected via a connection channel (6) to the outlet (23) of the compounder (2), wherein the twin screw (22) of the compounder (2) is designed as a co-rotating twin Screw (22) and the agglomerating tool (8) of the agglomerating vessel (11) is arranged in the fall direction of the mix below the connection channel (6) and comprises mutually engaging rotors (81) and stators (82) for producing agglomerates of defined particle size. The invention further relates to a method for producing polymer agglomerates. | ||||||
| 90 | HINGE DAMPENING DEVICE FOR GRANULATION BOWL LID | US14606436 | 2015-01-27 | US20160215546A1 | 2016-07-28 | Nicholas Decker; Nigel P. Wright |
| A hinge dampening device is provided for a granulation processor having a bowl and a lid. A dampening device includes first and second spaced apart hinge supports fixed to the bowl and a pin extending through the lid collar residing between the hinge supports. The first end of the pin is fixed to the first hinge support, and a second end of the pin extends through the second hinge support. An adjustable compressive force is applied axially to the hinge supports and lid collar to create frictional resistance to rotation of the lid. The rotational resistance provides controlled opening and closing of the lid. | ||||||
| 91 | APPARATUS AND METHOD FOR PRODUCING BIOBASED CARRIERS FROM BYPRODUCTS OF BIOMASS PROCESSING | US14939196 | 2015-11-12 | US20160135449A1 | 2016-05-19 | Klein E. Ileleji; Kyle V. Probst |
| An apparatus for producing biobased carriers for dispersal of biological and chemical molecules includes a premixer having a first inlet, a first outlet, a cavity configured for receiving a wet coproduct and a binder through the first inlet, and a stirring apparatus within the cavity for premixing the wet coproduct and binder into a substantially homogeneous mixture; a high shear mixer having a housing, a drive apparatus and a high shear apparatus, the housing defining an opening, the drive apparatus being within the housing and for forcing the substantially homogeneous mixture from the premixer into the high shear apparatus, and the high shear apparatus including a rotor, a stator and a screen covering the opening and being for shear mixing the mixture including forcing the mixture through the screen and out of the housing in the form of nucleation enhanced particles; and an agglomerator having an interior chamber sized and configured to receive the nucleation enhanced particles from the high shear mixer and for transforming the nucleation enhanced particles into substantially spherical biomass pellets. | ||||||
| 92 | Mixer of a rotor-stator type, performance estimation method thereof, and scale up method thereof | US13817094 | 2010-10-18 | US09278322B2 | 2016-03-08 | Tetsu Kamiya |
| Herein is disclosed a comprehensive mixer performance estimation method that can be applied to the mixers of the rotor-stator type having various configurations and circulation systems. Specifically, the performance estimation method for the mixers of the rotor-stator type includes the steps of: obtaining the homogenization index: H.I. for each of the mixers, measuring the size of each of the mixers, the power requirements and flow rates during the running time of each of the mixers, estimating the magnitude (smallness or greatness) of the configuration dependent term value of each of the mixer as a whole which is specific to each of the mixers, and estimating the performance of each of the mixers accordingly. | ||||||
| 93 | Powder treating apparatus | US12743732 | 2008-03-03 | US08876368B2 | 2014-11-04 | Takao Takasaki; Katsumi Kawai; Manabu Katayose; Norihiro Kon; Takashi Fujisaki; Kazunori Ozawa |
| There is provided a powder treating apparatus which can uniformly and successively combine and grow powders having different specific gravities or sizes together with a simple structure. The apparatus comprises a rotating container 20 into which plural kinds of powders P having different specific gravities or sizes are supplied and which rotates in a predetermined direction, a fixed container 30 retaining the rotating container 20, primary treating means M1 which is so arranged as to face an inner periphery surface 20S of the rotating container 20 and to extend in an axial direction, generates turbulence flow including eddying flow together with a rotational motion of the rotating container 20, and stirs and mixes the powders P having different specific gravities or sizes, a communicating hole 25 for ejecting the powders P stirred and mixed by the primary treating means M1 to a predetermined treatment space around the rotating container 20, and secondary treating means M2 which applies planar compressive shear force to the powders P ejected from the communicating hole 25 with an inner periphery surface 30S of the fixed container 30 to carry out a composite treatment, and causes the powders P having undergone a composite treatment to flow back in the rotating container. | ||||||
| 94 | Ingot mold for silicon ingot and method for making the same | US12694566 | 2010-01-27 | US08859034B2 | 2014-10-14 | Shigeru Gotoh; Youhei Sakai; Kentaro Okushima |
| A method for forming a mold comprises forming a body by kneading a ceramic powder comprising a silicon nitride powder and a first binder solution; forming a slurry by adding a second binder solution to the body; and forming a release layer by attaching the slurry to a surface of a mold base. A method for manufacturing a solar cell element comprises forming a silicon ingot by solidifying a silicon melt in the mold obtained by the above-described method for forming a mold; slicing the silicon ingot into substrates each having a predetermined thickness; forming a diffusion layer on each of the substrates; and forming an electrode on a surface of the diffusion layer. | ||||||
| 95 | Apparatus and Method for Packaging a Granulated Composition of Matter | US14212245 | 2014-03-14 | US20140263776A1 | 2014-09-18 | Francesco Bottura |
| The present invention relates, to a device for conditioning as granules a composition formulated from organic and mineral raw materials, characterized in that it comprises a rotary tank with a hyperbolic or exponential wall receiving the bulk raw materials in the upper portion, at least one set of blades ensuring the mixing and milling of said materials inside the tank and a helical groove borne by the wall of said tank and ensuring together delivery by centrifugation and guiding of the mixture from the low portion of the tank to its upper portion and gradual agglomeration of said materials in granules, on the one hand and, to a method for conditioning said composition by means of said device, on the other hand. | ||||||
| 96 | Kneading tank inversion discharging sealed pressurized type kneading machine | US13378985 | 2010-06-07 | US08764274B2 | 2014-07-01 | Yasuo Yada; Tatsuo Yada |
| A kneading machine is provided having a kneading tank with kneading rotors therein and a stocking opening. The kneading machine may also include a pressurizing lid for opening and closing the kneading tank and an inner-pressure cover. The kneading tank is capable of inverting in a range of 90° to 120° for discharging the kneaded materials. A front wall defining the stocking opening may be attached so as to be suspended downward from the kneading tank by a hinge when the kneading tank is inverted. The kneading machine may also include a capturing apparatus with a duct connected to the inner-pressure cover to capture powder compound jetted into the inner-pressure cover, and the powder compound captured in a filter of the capturing apparatus can be collected into the kneading tank. | ||||||
| 97 | Continuous granulator and method of continuous granulation of powder material | US11910690 | 2006-04-18 | US08708551B2 | 2014-04-29 | Ove Emil Hansen; Trevor Gordon Page; Michel Simon Waldron |
| A continuous granulator comprises a longitudinal granulation chamber having a first end with an inlet for powder material and a binder feed port and a second end with an outlet for granulated product. The granulation chamber comprises at least two parallel rotary shafts provided with granulating elements and forming an angle of from 0 to 70 degrees with the vertical. Each granulating element on a shaft comprises at least one lobe having limited extent in the circumferential direction of the shaft and interleaving with a lobe of a granulating element on another shaft. A plurality of such separate granulating elements are distributed from the inlet to the outlet, and successive granulating elements on a shaft are mutually angled. | ||||||
| 98 | METHODS AND SYSTEMS FOR COATING GRANULAR SUBSTRATES | US13984471 | 2012-02-09 | US20140033779A1 | 2014-02-06 | Marcus A. Bertin; Laurence G. Dammann; Robert M.A. Radabaugh; Arthur R. Shirley, JR.; Willem L.C. van Pol |
| The invention relates to methods and systems for coating substrates. In particular, the invention relates to methods and systems in which the coating and curing steps are performed in separate vessels. These methods and systems provide a more effectively controlled and efficient coating process. | ||||||
| 99 | GRANULATION BY AGGLOMERATION OF CERAMIC COMPOSITIONS GROUND IN DRY PHASE | US13881549 | 2011-10-25 | US20130248625A1 | 2013-09-26 | Antonio Arnau Villanova |
| The invention relates to the granulation by agglomeration of ceramic compositions ground in dry phase. The invention proposes an alternative to the method of wet-phase grinding and drying by atomization. The method consists of dry-phase grinding and preparing argillaceous ceramic compositions without binders, additives, or deflocculants from argillaceous minerals (about 60%) mixed with inorganic materials, grain sizes of less than 120 micrometers, in a horizontal rotary cylindrical device with deflecting paddles, the intake of said minerals, powdery materials and water takes place at one end of said device; and granules that are moved by said deflecting paddles are formed due to the rotation of said device. The outlet of the granulated material is at the opposite end of said device. The invention offers the following advantages: energy savings of 80%; savings in water consumption during granulation of 75-80% and 10-20% of additional savings in the pressure for pressing the granules. The time necessary to change from one ceramic composition to another is one hour, compared with several days using the current method of atomization. The method of granulation constitutes a novel environmental technology with zero air and water table pollution, and with much lower water consumption. | ||||||
| 100 | Process and apparatus for continuous wet granulation of powder material | US13009309 | 2011-01-19 | US08231375B2 | 2012-07-31 | Jean-Paul Remon; Chris Vervaet; Eseldin Keleb; An Vermeire |
| An apparatus for wet granulating a powder material comprises:—a barrel having a granulation chamber and being provided with a first inlet (1) for receiving said powder material and for supplying it to said granulation chamber and with a second inlet (2) for receiving a granulating liquid and for supplying it to said granulation chamber, said granulation having an aperture (9) for discharge of granules from said barrel, and—a transporting means (S) for advancing said powder material toward the end of said granulation chamber while granulating it with the aid of said granulating liquid, said transporting means (S) comprising a first transport zone (4) at its rear end, an agglomeration zone (5) downstream from the first transport zone (4) and a second transport zone (8) at its front end, said first inlet (1) and said second inlet (2) being positioned above the first transport zone (4), wherein said aperture (9) has a shape tightly fitting the terminal portion of the transporting means (S) for directly discharging said granules from the granulation chamber. The apparatus is useful for continuously wet granulating biologically-active ingredient formulations, chemicals, detergents and foodstuffs. | ||||||
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