| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 21 | 便于原料输送的塑料生产系统 | CN201610273575.X | 2016-04-27 | CN105729671A | 2016-07-06 | 朱树范 |
| 本发明涉及塑料加工设备技术领域，涉及一种便于原料输送的塑料生产系统。其包括依次连接的料仓、输料管道、称料机、混料机、临时料仓、挤出机、模面热切造粒机、第一旋风分离器、第二旋风分离器、振动筛和包装机；料仓包括构造成筒状的料仓本体，料仓本体侧面螺旋缠绕有通水管，料仓本体下部构造有与通水管连通的进水口，料仓本体上部构造有与通水管连通的出水口；输料管道包括管道本体，管道本体包括构造成柱状的管道主体，管道主体中部沿轴向构造有用于通入高温介质的加热流道，管道主体内沿轴向围绕加热流道地构造有至少一个用于通入物料的进料通道。本发明能够较佳地对原料进行加热，从而便于原料的抽取、输送。 | ||||||
| 22 | 用于形成厚热塑性复合结构的方法和设备 | CN201380055107.X | 2013-09-09 | CN104755252A | 2015-07-01 | R·D·威尔克森; J·R·福克斯 |
| 使用方法和设备预固结并压实热塑性复合层片堆叠(16)，之后完全固化并且成形成最终部件形状。预固结和压实是通过将层片堆叠(16)加热至低于热塑性复合层片的熔点的温度以软化层片(18)并且接着压制层片堆叠(16)来实现的。 | ||||||
| 23 | 实施传质处理的设备 | CN01821548.3 | 2001-12-14 | CN100398288C | 2008-07-02 | K·科尔格吕伯; F·维里希 |
| 本发明描述一种在高粘度液体中进行传质处理且尤其是聚合物熔体的浓缩和/或脱气的设备，它包括至少一个垂直放置的容器(1)，该容器(1)有一个用于输入待处理液体的供应装置(4)、用于挥发性成份的出口(7)和用于处理后液体的出口(6)，供应装置(4)有一个分配件(3)，它具有多个将待处理的高粘度液体分成多股单独液流的开口(8，10)，其特征在于，在开口(8，10)区域里安置着基本垂直布置的线环(2)，高粘度液体在重力作用下在线环上流走。 | ||||||
| 24 | 提高微细粒料密度的设备及方法 | CN02818163.8 | 2002-01-17 | CN1261328C | 2006-06-28 | 史蒂文·多普; 苏珊·戈尔德布卢姆; 贾里·詹森 |
| 一种用于排出微细粒料间空气的设备包括：一带一排气口(8)的料筒(1)；一料筒的进料口(2)；一料筒的出料口(5)；一在所述料筒(1)里旋转的螺旋体(4)；所述螺旋体适合于旋转以将所述粒料从所述进料口(2)输送至所述出料口(5)；一用于驱动所述螺旋体(4)的马达；和一压缩组件(6，7，9)，安装在所述出料口(5)处，用于压缩通过所述出料口的粒料。 | ||||||
| 25 | 可浇注液态介质的连续混合脱气的方法和装置 | CN95195762.7 | 1995-10-20 | CN1100653C | 2003-02-05 | 埃尔哈德·豪伊泽 |
| 本发明涉及可浇注液体介质的连续混合和脱气的方法，特别是对浇注用树脂组份或一种浇注用树脂组份以及填料诸如石英粉、氧化铝或染料进行连续混合和脱气的方法。本发明还涉及实施此方法的装置。为了向进一步的加工过程连续提供均匀的已脱气的浇注用树脂组份，液体组份或至少一种液体组份和填料按配料比输入连续脱气设备(1)中。 | ||||||
| 26 | 粒状填料的处理方法和装置 | CN00801937.1 | 2000-01-28 | CN1327411A | 2001-12-19 | J·克瑙德尔 |
| 本发明涉及处理粒状填料的方法和装置,以便接着生产诸如在污水工程中应用的玻璃纤维增强塑料管。 | ||||||
| 27 | 可浇注的液态介质，特别是浇注用树脂组份以及填料的连续混合和脱气方法 | CN95195762.7 | 1995-10-20 | CN1161664A | 1997-10-08 | 埃尔哈德·豪伊泽 |
| 本发明涉及可浇注液体介质的连续混合和脱气的方法，特别是对浇注用树脂组分或一种浇注用树脂组分以及填料诸如石英粉、氧化铝或染料进行连续混合和脱气的方法。本发明还涉及实施此方法的装置。为了向进一步的加工过程连续提供均匀的已脱气的浇注用树脂组分，液体组分或至少一种液体组分和填料按配料比输入连续脱气设备(1)中。 | ||||||
| 28 | Edible oral strip or wafer dosage form containing ion exchange resin for taste masking | US15420918 | 2017-01-31 | US20170136078A1 | 2017-05-18 | Michael LI; Markus KRUMME |
| An edible oral film strip dosage form containing an unpalatable basic active pharmaceutical ingredient and an ion exchange resin as a primary taste masking agent, along with an optional acidic agent and further optionally containing one or more secondary taste masking agents is provided. The edible oral film strip dosage matrix is formed from at least one water soluble or miscible polymer(s). The optional secondary taste masking ingredients include one or more of flavoring agent(s), sweetener(s), cooling sensation agent(s), and taste receptor blocker(s). Methods for preparing the inventive edible oral film strip dosage forms are disclosed, as well as their method of administration. | ||||||
| 29 | System and Method for Preparing, Dispensing and Curing Epoxy | US15010430 | 2016-01-29 | US20160144533A1 | 2016-05-26 | Keith Van Duinen; Miguel Rodriguez; Alejandro Leon |
| A method for dispensing epoxy comprising the step of degassing an epoxy. The method further comprises the step of associating the epoxy with an epoxy injector comprising a dispensing end. The method further comprises the step of a computer receiving data representative of a selected container to receive the epoxy. The method further comprises the step of a computer determining a dispensing rate and a dispensing amount, based on the received data. The method further comprises the step of a computer causing the epoxy injector to dispense the determined dispensing amount of epoxy, via the dispensing end, at the determined dispensing rate. The method further comprises the step of a computer causing a dispensing arm, supporting the dispensing end, to retract the dispensing end while the epoxy injector is dispensing the epoxy. The method further comprises the step of curing the dispensed epoxy. | ||||||
| 30 | Thin film in-line degasser | US10914549 | 2004-08-09 | US07717982B2 | 2010-05-18 | Kent A. Young; Stephen C. Pegram; Kerry T. Sanders |
| The present invention relates to a stackable packing element for use in degassing liquid ophthalmic lens monomer and a lens resulting therefrom. One or more stackable elements can be used to form a modular degasser and implement an in-line degassing process, employing same. The stackable packing element is comprised of a body module and a removable puck component. | ||||||
| 31 | Thin film in-line degasser | US10914549 | 2004-08-09 | US20090045532A1 | 2009-02-19 | Kent A. Young; Stephen C. Pegram; Kerry T. Sanders |
| The present invention relates to a stackable packing element for use in degassing liquid ophthalmic lens monomer and a lens resulting therefrom. One or more stackable elements can be used to form a modular degasser and implement an in-line degassing process, employing same. The stackable packing element is comprised of a body module and a removable puck component. | ||||||
| 32 | Apparatus and method for increasing density of finely divided particulate matter | US10878141 | 2004-06-28 | US20040256419A1 | 2004-12-23 | Steven Fred Dopp; Susan Jane Gelderbloom; Jary David Jensen |
| An apparatus for removing air from finely divided particulate material comprises a housing including a vent; an inlet to the housing; an outlet from the housing; a helix, rotatably mounted in the housing, the helix being adapted upon rotation to feed a particulate material from the inlet to the outlet; a motor mounted to the helix for the purpose of rotating the helix; and a compression assembly mounted to the outlet for compressing the particulate material passing through the outlet. | ||||||
| 33 | Method and apparatus for producing gas occlusion-free and void-free compounds and composites | US924382 | 1997-09-05 | US6009635A | 2000-01-04 | Victor H. Vidaurre; Jorge L. Dufeu; Wilfredo G. Bendek |
| The present invention discloses a generic method for producing void and gas occlusion free materials, as well as apparatuses for batch and continuous production of same. This generic method can be utilized in the production of a wide variety of polymeric compounds and composites and specifically encompasses the two ends of the polymeric composite spectrum, that is, polymer concretes on the one hand, and fiber-reinforced polymer composites on the other. The composite materials of the present invention are characterized by visual count as being void and gas occlusion free to the level of 1 micron at 1250.times. magnification. Concomitantly, the invention produces useful polymer concrete materials which exhibit substantially improved integrity for easy machining at high speeds, and high dielectric and mechanical strength, as compared with composite materials produced by conventional methods. Thus, one particularly well-suited application for the materials of the present invention is the class of high voltage electrical insulating materials and insulators where the presence of voids, or gas occlusion flaws, may have deleterious effects, leading to their early failure. | ||||||
| 34 | Degassing apparatus and method of the polymer powder | JP2008557750 | 2007-03-06 | JP5340747B2 | 2013-11-13 | ダム，エリック |
| The present invention relates to an apparatus for degassing polymer powder comprising a chamber (1) having a first end (20) and a second end (21) opposite to each other, said chamber (1) being equipped with at least one powder inlet and at least one gas outlet at the first end (20) and with at least one powder outlet and at least one gas inlet at the second end (21), and a valve (8) provided with a powder entry and a powder exit and arranged at the powder outlet (6) of said chamber. The apparatus is characterised in that said chamber (1) is equipped with a gas line (16) joining a gas exit of the valve (8) to the inside of the chamber (1) at a position that is at a distance h 2 from the first end (20), said distance h 2 being 20-80% of the height H of the chamber (1) and at a distance I 1 from a wall (22) of said chamber (1), said distance being I 1 0-50 % of the largest diameter L of the chamber (1). The invention also relates to a method for degassing polymer comprising flushing the polymer powder in a chamber with a flow of flushing gas, wherein at least a part of flushing gas exiting the chamber through a powder outlet is re-introduced into said chamber. | ||||||
| 35 | Apparatus and method for increasing the density of the atomized particulate matter | JP2003532358 | 2002-01-17 | JP4188834B2 | 2008-12-03 | ジャリー・ジェンセン; スーザン・ジェルダーブルーム; スティーブン・ドップ |
| 36 | Drawing up method for plastic product, membrane in-line type degassing method, and its apparatus | JP2005229658 | 2005-08-08 | JP2006051818A | 2006-02-23 | YOUNG KENT A; PEGRAM STEPHEN C; SANDERS KERRY T |
| PROBLEM TO BE SOLVED: To provide a degassing technique which improves effectiveness in both operation and maintenance, can be applied in in-line, and alleviates the problem of clearout. SOLUTION: This invention relates to a supplementary element which can be piled, is used in degassing a liquid ophthalmic lens monomer and relates to the lens obtained as a result. A module type degassing apparatus can be formed using an element which can be piled in at least one, and the in-line type degassing method using this can be implemented. The supplementary element which can be piled comprises a body module (10) and a pack component (20) which can be removed. COPYRIGHT: (C)2006,JPO&NCIPI | ||||||
| 37 | Method for producing a food contact grade polyethylene terephthalate resin from the waste pet container | JP2001524779 | 2000-09-18 | JP2003509249A | 2003-03-11 | コジオア，エドワード |
| (57)【要約】 ＰＥＴ材料と非ＰＥＴ材料を含有する廃棄物ストリームから食品接触グレードＰＥＴを製造する方法が開示されている。 この方法は、非ＰＥＴ材料の少なくとも一部を廃棄物ストリームから分別する工程と、その後、ＰＥＴ容器を好ましい最大サイズ約１０ｍｍのフレークに分割する工程と、その後、アルカリ材料および好ましくは非イオン性の界面活性剤を含有する高温水性媒体中で前記フレークを洗浄して、微粒子および吸収された異物を前記フレークの表面から除去する工程とを伴う。 この工程の後に、前記フレークを脱水し、その後、最大で０．１％ｗ／ｗ、より好ましくは最大で０．０１％ｗ／ｗの含水率に乾燥する工程が続く。 次の工程は、真空下、好ましくは１〜１０ミリバール（１００〜１０００Ｐａ）、より好ましくは２〜７ミリバール（２００〜７００Ｐａ）下で、ＰＥＴの融点より低い温度、好ましくは１７０〜２２０℃の範囲内の温度で、少なくとも３０分、好ましくは少なくとも６０分にわたり前記フレークを加熱するとともに激しく混合することにより、吸収された異物と水分を除去することを伴う。 最後の工程は、真空処理用に装備されたスクリュー押出機内で前記フレークを溶融することと、溶融材料を押し出してストランドを形成し、それをペレット化することを伴う。 | ||||||
| 38 | FURANOATE-BASED POLYESTER AND COPOLYESTER COMPOSITIONS USING FALLING STRAND DEVOLATILIZATION | US15780906 | 2016-12-02 | US20180346662A1 | 2018-12-06 | Ronald D. MOFFITT; Jasmeet KAUR |
| The present invention is directed to polymers and copolymers, and systems and methods for processing the same. Advantageously, the polymers and copolymers of the present invention have undergone processing in a falling strand devolatilizer and rotary disk finisher such that a low-cost, low-energy, and high-production-rate product is produced. | ||||||
| 39 | Devolatilisation apparatus and a process for use thereof | US14763707 | 2014-02-03 | US10143941B2 | 2018-12-04 | François Loviat |
| A static devolatilisation apparatus (1) adapted for devolatilising a viscous liquid (2) comprising a volatile component is disclosed. The apparatus (1) comprises a phase separation chamber (100) in an upper region (5) for treating the viscous liquid (2) in a first devolatilisation step to form a first devolatilised viscous liquid (21), and a distributor sub-unit 200 is located below the phase separation chamber (100) and above a lower sump region (4). The sub-unit (200) has a second discharge region (222) embodied such that it is contacted by the first devolatilised viscous liquid (21), and the region (222) has a surface (223) embodied such that the first devolatilised viscous liquid (21) is treated in a second devolatilisation step. The present invention further relates to a process to devolatilising a viscous liquid using the apparatus (1) and also to the use of the apparatus (1) in the devolatilisation of polymer melt or solution. | ||||||
| 40 | High Molecular Weight Polyamides and CoPolyamides with Uniform RV and Low Gel Content | US15778778 | 2016-11-29 | US20180340042A1 | 2018-11-29 | James E. Polk; Chris E. Schwier; Ashish Sen; Craig A. Trask; Cihan Uzunpinar; Chie-Hsiung Wang; J. Marty Zabcik |
| A customizable polyamide polymer, in particular Nylon 66, Nylon 6, and copolyamides, having a high molecular weight, excellent color, and low gel content is disclosed. In particular, disclosed is a polymer having a relative viscosity greater than 50 as measured in a 90% strength formic acid solution; consistent viscosity with a standard deviation of less than 1; a gel content no greater than 50 ppm as measured by insolubles larger than 10 micron; an optical defect content of less than 2,000 parts per million (ppm) as measured by optical control system (OCS). The polymer can be made into monofilaments or a multifilament yarn.Also disclosed is a process of producing the polymer using in-line vacuum finishing technology in the absence of steam or other gases in the second, or post condensation, step of the polymer process. | ||||||
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