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1.发明申请Fluidized bed process having a hydro dynamically active layer and a method for use thereof 审中-公开具有水动力活性层的流化床方法及其使用方法公开(公告)号：US20050091873A1
公开(公告)日：2005-05-05
申请号：US11003646
申请日：2004-12-06
申请人： Roman Maryakhin
发明人： Roman Maryakhin
IPC分类号： B01F13/02 , B01J2/16 , B01J8/24 , B01J8/32 , B01J8/36 , B01J8/38 , B01J8/44 , F26B3/088 , F26B3/092 , F26B3/08 , A23G3/00
CPC分类号： B01F13/0255 , B01J2/16 , B01J8/1872 , B01J8/245 , B01J8/32 , B01J8/36 , B01J8/386 , B01J8/44 , F26B3/088 , F26B3/0926
摘要： The present invention relates to fluid bed processors used in various industries for drying, coating, agglomerating, and performing other specific processes on particle materials. The processor is especially useful for processing particles, utilizing a hydro dynamically active layer (HDAL) produced by introducing a high speed gas jet through said particulate material under controlled conditions. The processor is adapted to be implemented in a plurality of different fluid bed applications and results in much more efficient particle processing, and a significant savings in energy consumption. The present invention also relates to a method comprising the steps of introducing particulate material into the processing chamber and passing a high-speed jet gas through a plurality of nozzles located in the base of said processing chamber, thereby producing distinct regions of low pressure so as to create an intense, substantially circulatory pattern of gas circulation into which said particulate material is picked up.
摘要翻译： 本发明涉及用于各种工业中用于干燥，涂覆，附聚和在颗粒材料上执行其它具体方法的流化床处理器。 处理器特别适用于处理颗粒，利用通过在受控条件下引入高速气体射流通过所述颗粒材料而产生的水力动态活性层（HDAL）。 该处理器适于实现在多个不同的流化床应用中并且导致更加有效的粒子处理，并且显着地节省了能量消耗。 本发明还涉及一种方法，其包括以下步骤：将颗粒材料引入处理室并使高速喷射气体通过位于所述处理室底部的多个喷嘴，从而产生不同的低压区域，以便 以产生气体循环的强烈的，基本上循环的图案，其中拾取所述颗粒材料。
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公开(公告)号：US20050050761A1
公开(公告)日：2005-03-10
申请号：US10714598
申请日：2003-11-18
申请人： Marzouk Benali , Mouloud Amazouz
发明人： Marzouk Benali , Mouloud Amazouz
CPC分类号： F26B3/0926 , F26B3/088
摘要： A jet spouted fluidised bed drier is described in which the bottom half of the drier chamber comprises a first lower conical part, and the top half of the drier chamber comprises a second upper conical part surrounding a conical grid located near to the top end of the second part. The drier chamber thus comprises two conical parts connected together at their wide ends. The result of this arrangement is that the collision zone becomes a toroid with an essentially triangular cross-sectional shape defined essentially by the conical internal surface of the top part and the conical outer surface of the conical grid. This revised structural arrangement has been found to be able to process materials which either cannot be processed, or cannot be processed efficiently, with known jet spouted fluidised bed driers. Additionally, this revised structural arrangement has been found to be able to process materials more efficiently, and to a lower desired final liquid content values.
摘要翻译： 描述了喷射流化床式干燥器的喷射器，其中干燥室的下半部分包括第一下部锥形部分，并且干燥器室的上半部分包括围绕位于第二下部锥形部分的顶端附近的圆锥形格栅的第二上部锥形部分 第二部分。 因此，干燥室包括在其宽端连接在一起的两个锥形部分。 这种布置的结果是碰撞区域成为基本上由顶部的锥形内表面和圆锥形格栅的圆锥形外表面确定的基本上三角形横截面形状的环形面。 已经发现这种修改的结构布置能够使用已知的喷射流化床式干燥器处理不能被加工或不能有效地加工的材料。 此外，已经发现，这种修改的结构布置能够更有效地处理材料，并且能够达到较低的期望的最终液体含量值。
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3.发明授权
公开(公告)号：US5913588A
公开(公告)日：1999-06-22
申请号：US928808
申请日：1997-09-12
申请人： Robert Legros , Jamal Chaouki , Xiao Tao Bi , Arturo Macchi , Kebir Ratnani
发明人： Robert Legros , Jamal Chaouki , Xiao Tao Bi , Arturo Macchi , Kebir Ratnani
CPC分类号： F26B3/088 , F26B23/022 , F26B3/0926 , F26B3/205 , Y02P70/40 , Y10S159/03 , Y10S159/901
摘要： A spout-fluid bed drying system and process is comprised of a spout-fluid bed dryer having a conical shaped lower section provided with a packing of heat exchange particles. A cyclone separator is connected to the top of the dryer with separated particles collected by a receiver connected to the leg of the cyclone. A vapor fan compresses the air-vapor mixture before it goes to the heat recuperator and mixing chamber. A tube-shell type heat exchanger, wherein effluent gases from the vapor fan are preheated with heat exchange with the outcoming high temperature gases. A combustion and incineration chamber wherein a natural gas burner is installed at the top and the high temperature flame is used to incinerate the effluent gases introduced from the annulus channel of the chamber to have the odors and VOCs destroyed. A mixing chamber wherein high temperature stream from the incineration chamber is mixed with low temperature stream from the vapor fan to serve as the drying media with the temperature maintained at around 400.degree. C. A slurry discharge nozzle is disposed below the packing and connected to a slurry container via piping and a slurry pump for releasing slurry to the surface of the particles within the packing. Evaporation of water occurs mostly on the surface of particles by contact with hot drying media. A gas-air mixture is fed to the burner through a feed pipe line wherein fresh air is supplied from an air blower.
摘要翻译： 喷口流化床干燥系统和方法由具有锥形下部的喷口流化床干燥器组成，其具有热交换颗粒的填料。 旋风分离器连接到干燥器的顶部，分离的颗粒由连接到旋风分离器的腿部的接收器收集。 蒸汽风扇在空气 - 蒸气混合物进入热交换器和混合室之前进行压缩。 管壳型热交换器，其中来自蒸气风扇的流出气体与输出的高温气体进行热交换而被预热。 一种燃烧和焚烧室，其中天然气燃烧器安装在顶部，高温火焰用于焚化从室的环形通道引入的废气以使臭味和VOC被破坏。 混合室，其中来自焚烧室的高温物流与来自蒸气风扇的低温流混合，用作温度保持在约400℃的干燥介质。浆料排出喷嘴设置在填料下方并连接到 通过管道的浆料容器和用于将浆料释放到填料内的颗粒表面的浆料泵。 水的蒸发主要发生在与热干燥介质接触的颗粒表面。 通过进料管线将气体 - 空气混合物供给到燃烧器，其中新鲜空气从鼓风机供应。
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4.发明授权公开(公告)号：US09788566B2
公开(公告)日：2017-10-17
申请号：US14902901
申请日：2014-01-27
发明人： Marzouk Benali
CPC分类号： A23L3/46 , A23P10/40 , A23V2002/00 , B01D1/18 , B01D1/20 , F26B3/088 , F26B3/0926 , F26B3/12 , F26B3/205
摘要： A system for producing free-flowing powder with a narrow particle size distribution from liquid compositions comprising in combination: a feeding reservoir comprising said liquid compositions: a pumping device to pump said liquid composition into at least one atomizing device: said at least one atomizing device composed of at least one fluid nozzle to distribute an upward gaseous drying medium over said nozzle: two lateral streamlined tube-like devices for supplying said liquid composition and pressurized gas to said at least one nozzle from two opposite directions: a cylindrical plenum chamber wherein the fluid nozzle is located: an accelerating zone of a drying medium consisting of a cylindrical pipe located at the bottom of the cylindrical plenum: a conical-cylindrical drying chamber equipped with a manhole, a multi-nozzle manifold and insulation panels: and an intermediate drying medium consisting of a single bed or multi-beds of inert carriers within the drying chamber.
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公开(公告)号：US4104806A
公开(公告)日：1978-08-08
申请号：US802697
申请日：1977-06-02
申请人： Robert J. Reusch
发明人： Robert J. Reusch
CPC分类号： F26B3/088
摘要： An improved method of drying particulate matter, subject to agglomeration, by fluidized bed drying is disclosed. The improvement of the method comprises adding an effective amount of a fluidizing agent to the particulate matter prior to drying.
摘要翻译： 公开了通过流化床干燥来干燥颗粒物质，经过聚集的改进方法。 该方法的改进包括在干燥之前向颗粒物质中加入有效量的流化剂。
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公开(公告)号：US3921307A
公开(公告)日：1975-11-25
申请号：US31776572
申请日：1972-12-29
摘要： This specification discloses a carboniser for coal compacts comprising a treatment channel containing a bed of particulate carrier which is fluidized intermittently or continuously by means of fluid distributor pipes arranged near the bottom of the channel. The channel has a feed section, a treatment section and a discharge section and is connected with a reheater for the carrier. The carrier is transferred between the channel and the reheater by means of downcomers and carrier lifters, the introduction of carrier being near the bottom of the channel and its removal being near the top of the bed so that the carrier passes upwardly through the channel in a direction which is transverse to the direction of transport of the compacts and carrier. When the compacts and some carrier are discharged from the treatment channel, the carrier is separated from the compacts and returned to the feed section. The specification also describes a special feed section arrangement which reduces emission of pollutants at the point of introduction of the compacts to the treatment channel.
摘要翻译： 本说明书公开了一种用于煤压块的碳化器，包括含有颗粒载体床的处理通道，其通过布置在通道底部附近的流体分配器管道间歇地或连续流化。 通道具有进料部，处理部和排出部，并与载体的再热器连接。 载体通过降液管和载物升降器在通道和再热器之间转移，载体靠近通道的底部并且其移除靠近床的顶部，使得载体向上通过通道 方向横向于压块和载体的输送方向。 当压块和一些载体从处理通道排出时，载体与压块分离并返回到进料段。 本说明书还描述了一种特殊的进料部分布置，其在将压块引入处理通道时减少了污染物的排放。
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7.发明授权Method in drying of hydrous solid material and the subsequent heat treatment of the dried material 失效水泥固体材料的干燥方法和干燥材料的后续加热处理
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8.发明授权
公开(公告)号：US5899003A
公开(公告)日：1999-05-04
申请号：US513752
申请日：1996-10-30
申请人： Ingvald Strommen , Kjartan Kramer , Ola Jonassen
发明人： Ingvald Strommen , Kjartan Kramer , Ola Jonassen
CPC分类号： F26B3/088 , F26B21/086 , F26B3/084
摘要： A method and apparatus for drying of a material containing a volatile component, in which the material is disposed in a bed in a drying zone which is in communication with a closed circuit in which a gaseous drying medium is circulated. Associated with the drying gone is a closed heat pump system including a compressor, at least one condenser in the drying zone, a super heat exchanger and a working medium. The drying zone is supplied with super heat from the super heat exchanger, and the condenser is supplied with working medium from a super heat exchanger, thereby increasing the temperature in the drying zone.
摘要翻译： PCT No.PCT / NO94 / 00049 Sec。 371日期1996年10月30日 102（e）日期1996年10月30日PCT 1994年3月1日PCT公布。 WO94 / 20804 PCT出版物 日期1994年9月15日一种用于干燥含有挥发性成分的材料的方法和装置，其中将材料设置在干燥区中的床中，该干燥区与气态干燥介质循环的闭合回路连通。 与干燥相关的是封闭的热泵系统，包括压缩机，干燥区中的至少一个冷凝器，超热交换器和工作介质。 干燥区由超级热交换器提供超热，冷凝器由超级热交换器供给工作介质，从而提高干燥区的温度。
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公开(公告)号：US4738828A
公开(公告)日：1988-04-19
申请号：US845666
申请日：1986-03-28
申请人： Edward F. Brooks
发明人： Edward F. Brooks
CPC分类号： B82Y30/00 , B01J8/1872 , C01F7/021 , C01G49/02 , D01F9/1278 , F26B3/088 , F27B15/00 , B01J2208/00681 , C01P2004/03 , C01P2004/61 , C01P2006/10
摘要： Tendrillar carbonaceous material is used as a fluidization aid for fluidized beds. The tendrillar carbonaceous material can be used to fluidized cohesive solids. Further, it can be used to improve fluidization of particulate solids by reducing entrainment, eliminating bubbling, and/or eliminating channelling. The tendrillar carbonaceous material can be a fibrous, particulate carbonaceous material comprising carbon fibers and a ferrous group metal component dispersed throughout the carbon fibers as nodules. The tendrillar carbonaceous material has a bulk density of from about 0.01 to about 0.7 g/cm.sup.3 and comprises an agglomeration of tendrils having a diameter of from about 0.01 to about 1 micron and a length to diameter ratio of from about 5:1 to about 1000:1.
摘要翻译： 藤本碳质材料用作流化床的流化助剂。 花柱碳质材料可用于流化粘性固体。 此外，其可以用于通过减少夹带，消除起泡和/或消除通道来改善颗粒固体的流化。 花岗岩含碳材料可以是包含分布在整个碳纤维中的碳纤维和亚铁族金属成分作为结核的纤维状颗粒状碳质材料。 花质碳质材料的堆积密度为约0.01至约0.7g / cm 3，并且包含直径为约0.01至约1微米并且长径比为约5:1至约1000的卷须的附聚 ：1。
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公开(公告)号：US4617272A
公开(公告)日：1986-10-14
申请号：US603711
申请日：1984-04-25
申请人： Marda K. Kirkwood , Keith E. Olson
发明人： Marda K. Kirkwood , Keith E. Olson
CPC分类号： C12N9/98 , F26B3/088 , F26B3/205 , Y10S435/803 , Y10S435/804
摘要： A process for removing the water from an enzyme-containing aqueous medium is disclosed which comprises spraying the medium onto a heated, fluidized bed of inert substrate particles and recovering a dry enzyme concentrate therefrom.
摘要翻译： 公开了一种从含酶水性介质中除去水的方法，其包括将介质喷洒到加热的惰性底物颗粒流化床上并从其中回收干燥的酶浓缩物。
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