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Method and device for introducing catalyst particles into a fluidized bed catalytic reactor

机译:将催化剂颗粒引入流化床催化反应器的方法和装置

摘要

The upstream part of the cracker contains at least one solid fixed packing (6) extending over all or part of the cracker cross section and forming a network of cells through which the catalyst particles pass. The network ensures at least one division and recombination of the catalyst particle flow to homogenize them over the cracker cross section. The catalytic cracker (1) contains fluid in its upstream part, and has at least one device (2) for supplying at least partly regenerated catalyst particles and at least one device (8) for injecting the load to be cracked. The packing is placed in the upstream part of the cracker, between the catalyst supply zone and the zone where the load to be cracked is injected. The cells in the packing are orientated radially to the gas and particle flow. At least part of the packing is in the form of static mixers. About 50% of the cells point in one direction and about 50% in a second direction which is at 10-90 degrees to the first. The packing is made of a series of corrugated plates cut across their corrugations and linked or welded so the peak of each corrugation forms an angle of 45-135 degrees , preferably 90 degrees to the peak of the corrugation of the next plate. At least part of the packing is made of one or more fragments of helix, juxtaposed and rotated relative to each other. At least part of the packing is a mesh or made of crossed bars stacked and welded to each other. The device contains at least two, preferably two-four packing elements as above, the same or assorted, juxtaposed or spaced out. The packing elements are made of heat and erosion resistant materials such as refractory steel or ceramic, and are arranged to handle fluidized catalyst particles at a density of 200-800 kg/m3. Downstream of the packing are deflectors to send the particles down the middle or the sides of the reactor. The deflectors have circular profiles and are annular or helical, or are rounded, hyperbolic, semicircular or semi-elliptical.
机译:裂化器的上游部分包含至少一个固体固定填料(6),其在裂化器的全部或部分横截面上延伸并形成催化剂颗粒通过的孔的网络。该网络确保了催化剂颗粒流的至少一种划分和重新结合,以使它们在裂化器横截面上均匀化。催化裂化器(1)在其上游部分中包含流体,并且具有至少一个用于供应至少部分再生的催化剂颗粒的装置(2)和至少一个用于注入要裂化的负载的装置(8)。填料被放置在裂化器的上游部分,在催化剂供应区和要裂化的负载被注入的区之间。填料中的小室径向地面向气流和颗粒流。填料的至少一部分是静态混合器的形式。大约50%的单元指向一个方向,大约50%指向第二方向,该方向与第一个方向成10-90度。填料由一系列瓦楞板制成,这些瓦楞板横切其瓦楞板并连接或焊接,因此每个瓦楞板的峰顶与下一块瓦楞板的峰顶形成45-135度的角度,最好为90度。填充物的至少一部分由一个或多个螺旋碎片构成,彼此并列并相对旋转。填料的至少一部分是网状或由相互堆叠并焊接在一起的交叉杆制成。所述装置包含至少两个,优选地如上所述的相同或分类,并置或间隔开的包装元件的2-4个。填充元件由诸如耐火钢或陶瓷的耐热和抗腐蚀材料制成,并且被布置成以200-800kg / m 3的密度处理流化的催化剂颗粒。填料的下游是导流板,用于将颗粒向下输送到反应器的中部或侧面。偏转器具有圆形轮廓并且是环形或螺旋形的,或者是圆形的,双曲线的,半圆形的或半椭圆形的。

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