Process and apparatus for the gas-phase polymerization of &agr;-olefins
    2.
    发明授权
    Process and apparatus for the gas-phase polymerization of &agr;-olefins 失效
    α-烯烃气相聚合的方法和装置

    公开(公告)号:US06413477B1

    公开(公告)日:2002-07-02

    申请号:US08943748

    申请日:1997-10-03

    Abstract: Process for gas-phase polymerization carried out in two interconnected polymerization zones, to which one or more &agr;-olefins CH2═CHR are fed in the presence of catalyst under reaction conditions and from which the polymer product is discharged. The process is characterized in that the growing polymer flows through a first polymerization zone under fast fluidization conditions, leaves said first zone and enters a second polymerization zone through which it flows in a densified form under the action of gravity, leaves said second zone and is reintroduced into the first polymerization zone, thus establishing a circulation of polymer around the two polymerization zones. The novel process allows olefins to be polymerized in the gas phase with high productivity per unit volume of the reactor without incurring the problems of the fluidized-bed technologies of the known state of the art.

    Abstract translation: 在两个相互连接的聚合区中进行气相聚合的方法,一个或多个α-烯烃CH 2 = CHR在催化剂存在下在反应条件下进料,聚合物产物从其中排出。 该方法的特征在于,生长的聚合物在快速流化条件下流过第一聚合区,离开所述第一区并进入第二聚合区,通过该第二聚合区,其在重力作用下以致密化形式流动,离开所述第二区,并且是 重新引入第一聚合区,从而建立聚合物周围两个聚合区的循环。 该新方法允许烯烃在气相中以每单位体积的反应器的高生产率聚合,而不会引起现有技术的流化床技术的问题。

    Stripping and separating apparatus and its use in fluidised bed catalytic cracking
    3.
    发明授权
    Stripping and separating apparatus and its use in fluidised bed catalytic cracking 有权
    剥离和分离装置及其在流化床催化裂化中的应用

    公开(公告)号:US06296812B1

    公开(公告)日:2001-10-02

    申请号:US09243116

    申请日:1999-02-03

    Abstract: An apparatus for separating and stripping a mixture of gas and particles comprises an envelope having separation chambers and circulation chambers distributed about a reactor, the upper portion of each separation chamber comprising an inlet opening communicating with the reactor and with a zone for rotating the mixture in a vertical plane. Each separation chamber comprises two lateral walls which are also walls for the circulation chamber, at least one of the walls of each chamber comprising a lateral outlet opening for mixing gas and particles into the adjacent circulation chamber. Each separation chamber also comprises an axial opening for particles to enter a stripping chamber, the envelope further comprises a conduit for evacuating a gas-particle mixture connected to at least one secondary separator and the stripping chamber communicating with the conduit via circulation chambers. Application of this apparatus is to fluidized bed catalytic cracking of hydrocarbons in a riser and/or dropper.

    Abstract translation: 用于分离和汽提气体和颗粒的混合物的装置包括具有分隔室和围绕反应器分布的循环室的外壳,每个分离室的上部包括与反应器连通的入口和用于使混合物旋转的区域 垂直平面 每个分离室包括两个侧壁,其也是用于循环腔的壁,每个室的至少一个壁包括用于将气体和颗粒混合到相邻的循环腔中的侧向出口。 每个分离室还包括用于进入汽提室的颗粒的轴向开口,所述外壳还包括用于排出连接到至少一个次级分离器的气体 - 颗粒混合物的导管和通过循环腔与导管连通的汽提室。 该设备的应用是在提升管和/或滴管中的烃类的流化床催化裂化。

    Hydrocarbon synthesis reactor employing vertical downcomer with gas disengaging means
    4.
    再颁专利
    Hydrocarbon synthesis reactor employing vertical downcomer with gas disengaging means 有权
    采用具有气体分离装置的垂直降液管的烃合成反应器

    公开(公告)号:USRE37229E1

    公开(公告)日:2001-06-12

    申请号:US09133423

    申请日:1998-08-13

    Abstract: The operation of a hydrocarbon synthesis reactor and catalyst distributed in the reaction slurry therein are improved by the presence in said reactor of one or more vertical downcomers open at both ends with gas disengaging areas located at their top end. The downcomer which circulates catalyst from the top of the reaction slurry to the bottom of said slurry is fully immersed in the reaction slurry and preferably extends from just above the bottom of the reaction zone of the reaction vessel to just below the top surface of the reaction slurry. The bottom end of said downcomer is shielded from intrusion of rising synthesis gas by the placement of a baffle which blocks rising gas entry but facilitates the exit of catalyst and liquid from the bottom of said downcomer and distributes them radially throughout the adjacent reactor slurry.

    Abstract translation: 通过在位于其顶端的气体分离区域的两端开放的一个或多个垂直下降管的所述反应器中存在分布在其中的反应浆料中的烃合成反应器和催化剂的操作。 将催化剂从反应浆料的顶部循环到所述浆料的底部的降液管完全浸入反应浆料中,优选从反应容器的反应区的正上方延伸到反应的顶部表面正下方 泥浆。 所述降液管的底端通过放置阻挡上升气体进入的挡板而防止上升的合成气的入侵,但有利于催化剂和液体从所述降液管的底部排出并将其径向分布在相邻的反应器浆料中。

    Apparatus and method for absorbing and recycling material in a blender
    5.
    发明授权
    Apparatus and method for absorbing and recycling material in a blender 失效
    在搅拌机中吸收和回收材料的装置和方法

    公开(公告)号:US06783743B1

    公开(公告)日:2004-08-31

    申请号:US09521748

    申请日:2000-03-09

    CPC classification number: B65G53/08 B01F15/00954 B01F15/00993 B01F15/0235

    Abstract: An apparatus and method for blending a solute and a solvent to form a solution product which substantially eliminates starting material and product operational loss while improving environmental safety both in the workplace and the ambient atmosphere. The apparatus and method employ a closed system and controls which remove substances from the overhead vapors generated in the various units by employing separate and distinct filtering systems. A high efficiency particulate air filter (HEPA) is employed in a closed solute supply means. A demister device is in fluid communication with the vent of the mixing vessel unit to remove solvent and solution products, to form droplets from the exhaust stream and return them to the mixing tank and discharging the exhaust stream without stress to the environment.

    Abstract translation: 一种用于混合溶质和溶剂以形成溶液产品的装置和方法,其基本上消除了起始材料和产品操作损失,同时改善了工作场所和环境大气中的环境安全性。 该装置和方法采用封闭系统并且控制哪些通过采用分离和不同的过滤系统从各种单元中产生的塔顶蒸气去除物质。 在封闭溶质供应装置中采用高效颗粒空气过滤器(HEPA)。 除雾器装置与混合容器单元的排气口流体连通以除去溶剂和溶液产物,以从排气流中形成液滴并将其返回到混合罐中并排出废气流而不受环境压力。

    Reaction process in hybrid reactor for propylene ammoxidation
    6.
    发明授权
    Reaction process in hybrid reactor for propylene ammoxidation 失效
    用于丙烯氨氧化的混合反应器中的反应过程

    公开(公告)号:US06649130B1

    公开(公告)日:2003-11-18

    申请号:US09635953

    申请日:2000-08-10

    Abstract: A hybrid reactor arrangement provides a reactive design that achieves higher acrylonitrile yield and lower catalyst circulating rate. The hybrid reactor design first passes a mixture of reactants and catalyst through a circulating bubbling bed reaction section. Heat exchange coils or other cooling medium in the bubbling bed reactor section maintain temperature in a range that will maximize the selectivity of reactants to the acrylonitrile product. The bubbling bed reactor section provides the initial conversion of the reactant. A circulating fluidized bed reaction zone finishes the conversion of reactants to a high yield under conditions that reduce the occurrence of secondary reactions that could otherwise produce unwanted by-products. The circulating fluidized bed reactor section maintains nearly plug flow conditions that allow continued conversion of unreacted feed components through primary reactions while limiting the time for secondary reactions to continue and diminish the final yield of products. Selectivity and conversion may also be improved by sequential addition of oxygen into the CFB reaction section. The sequential addition of oxygen may occur by the direct injection of an oxygen-containing gas or by the delivery of re-oxidized catalyst particles that are fully recharged with the lattice oxygen necessary for the reaction. Through this method the hybrid reactor provides the typical 5% improvement of higher acrylonitrile product yield from CFB-type reaction zones while reducing the required catalyst circulation by a factor of 10 or more.

    Abstract translation: 混合反应器装置提供了实现较高丙烯腈产率和较低催化剂循环速率的反应性设计。 混合反应器设计首先将反应物和催化剂的混合物通过循环鼓泡床反应段。 鼓泡床反应器部分中的热交换盘管或其它冷却介质将温度保持在使反应物对丙烯腈产物的选择性最大化的范围内。 起泡床反应器部分提供反应物的初始转化。 循环流化床反应区在减少可能产生不需要的副产物的次级反应的情况下,完成反应物转化为高收率。 循环流化床反应器部分保持几乎堵塞流动条件,其允许未反应的进料组分继续转化通过初级反应,同时限制二级反应的持续时间并降低产物的最终产率。 还可以通过将顺序加入到CFB反应部分中来提高选择性和转化率。 氧的顺序添加可以通过直接注入含氧气体或通过输送用反应所需的晶格氧充分再充电的再氧化的催化剂颗粒进行。 通过该方法,混合反应器提供了CFB型反应区中较高丙烯腈产物产率的典型的5%的改进,同时将需要的催化剂循环减少10倍或更多。

    Plant for continuously regenerating foundry sand and associated method
    8.
    发明授权
    Plant for continuously regenerating foundry sand and associated method 有权
    用于连续再生铸造砂和相关方法的工厂

    公开(公告)号:US06399032B1

    公开(公告)日:2002-06-04

    申请号:US09371859

    申请日:1999-08-11

    Inventor: Bartolomeo Tosco

    CPC classification number: B22C5/08 B01J8/1818

    Abstract: The plant for continuously regenerating foundry sand comprises a combustion chamber, in which a combustible gas is added to the sand, and a cooling chamber, in which the sand coming from the combustion chamber is cooled, both chambers being provided with systems for maintain the sand in a fluidized state. The chambers are also in direct communication with one another in the manner of communicating vessels in such a way that, during normal operation in equilibrium, the free surface of the sand may be at the same level in the two chambers.

    Abstract translation: 用于连续再生的铸造砂的设备包括其中将可燃气体添加到砂中的燃烧室和其中来自燃烧室的砂被冷却的冷却室,两个室都设有用于保持砂的系统 处于流化状态。 这些室也以彼此连通的方式彼此直接连通,使得在平衡的正常操作期间,砂的自由表面可以在两个室中处于相同的水平。

    Apparatus for gas-phase polymerization
    9.
    发明授权
    Apparatus for gas-phase polymerization 有权
    气相聚合装置

    公开(公告)号:US06818187B2

    公开(公告)日:2004-11-16

    申请号:US10680624

    申请日:2003-10-07

    Abstract: An apparatus for gas-phase catalytic polymerization comprising a first vertical reactor (1), a second vertical reactor (2), the upper region of said reactor (1) being connected by a connecting part (3) to a solid as separator (4), which is in turn connected to the upper region of second reactor (2), the lower region of second reactor (2) being connected to the lower region of first reactor (1) by a connecting part (5), the solid/gas separator (4) being connected through a recycle line (6) to one or more points of reintroduction into connecting part (5) or into reactor (1), the apparatus having a line (12) for feeding catalyst into reactor (1), a polymer discharge system (11) from reactor (2), a line (13) for feeding monomers, the apparatus being further characterized in that it comprises a line (15) for feeding gas or liquid into reactor (2).

    Abstract translation: 一种用于气相催化聚合的装置,包括第一垂直反应器(1),第二垂直反应器(2),所述反应器(1)的上部区域通过连接部分(3)连接到作为分离器(4)的固体 ),其又连接到第二反应器(2)的上部区域,第二反应器(2)的下部区域通过连接部分(5)连接到第一反应器(1)的下部区域,固体/ 气体分离器(4)通过再循环管线(6)连接到再连接到连接部分(5)或反应器(1)中的一个或多个点,该设备具有用于将催化剂进料到反应器(1)中的管线(12) ,来自反应器(2)的聚合物排出系统(11),用于供给单体的管线(13),该装置的进一步特征在于其包括用于将气体或液体进料到反应器(2)中的管线(15)。

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