首页> 外国专利> REACTOR EXCHANGER TUBES BAIONNETTES AND A TUBE OF SMOKE SUSPENDED TO THE SUPERIOR REACTOR OF THE REACTOR

REACTOR EXCHANGER TUBES BAIONNETTES AND A TUBE OF SMOKE SUSPENDED TO THE SUPERIOR REACTOR OF THE REACTOR

机译:反应器交换管的网状结构和悬挂在反应器高级反应器中的烟管

摘要

The reactor exchanger comprises a cylindrical shell (1) closed by a vaulted ceiling (2) and a lower bottom (3). The set of shell, lower bottom and vaulted ceiling are coated with a refractory insulation coating. The shell encloses bayonet tubes parallel to the vertical axis extending from the bottom of the shell until the vaulted ceiling, within which the reactional fluid flows. Each bayonet tube is surrounded along the entire length of smoke tubes. The inlet and outlet of each bayonet tube extends outside the reactor beyond the vaulted ceiling. The reactor exchanger comprises a cylindrical shell (1) closed by a vaulted ceiling (2) and a lower bottom (3). The set of shell, lower bottom and vaulted ceiling are coated with a refractory insulation coating. The shell encloses bayonet tubes parallel to the vertical axis extending from the bottom of the shell until the vaulted ceiling, within which the reactional fluid flows. Each bayonet tube is surrounded along the entire length of smoke tubes. The inlet and outlet of each bayonet tube extends outside the reactor beyond the vaulted ceiling. The hot gases are generated outside the reactor, introduced inside the shell with an opening in the lower bottom, and then enter in the smoke tubes with drilled holes for admission to their walls and leave the smoke tubes by discharge openings arranged at its top and through a side opening. Each bayonet tube and the smoke tube are suspended from the vaulted ceiling of the heat exchanger reactor by a system of clamps. The spacing between each bayonet tube, or center to center distance is 2-5 times the inside diameter of outer tube. Each smoke tube is divided into an upper ceramic metal and a lower ceramic metal. A refractory brick arch is used for covering the entire section of the heat exchanger reactor, and is located at the junction between the upper and lower ceramic metal parts of the fire tubes allowing the passage of the smoke tubes. A sealing plate is located at the top of the heat exchanger reactor tubes and attached to the smoke tube. The smoke tubes are fitted in the lower part of the openings located below the level of the shell and in their upper part with drain holes located above the sealing plate. The density of the bayonet tube is 2-12 tubes/m 2section of the reactor. The sealing plate has number of folds to ensure its own thermal expansion. Independent claims are included for: (1) a process for steam reforming a hydrocarbon fraction using a heat exchanger reactor; and (2) a process for assembling the heat exchanger reactor.
机译:反应器交换器包括由拱形顶板(2)和下部底部(3)封闭的圆柱形壳体(1)。外壳,下部底部和拱形天花板均涂有耐火隔热涂层。壳体包围平行于垂直轴的卡口式管,该垂直轴从壳体的底部一直延伸到拱形顶棚,反应流体在拱顶内流动。每个刺刀管沿烟管的整个长度围绕。每个刺刀管的入口和出口延伸到反应堆外部,超过拱形顶棚。反应器交换器包括由拱形顶板(2)和下部底部(3)封闭的圆柱形壳体(1)。外壳,下部底部和拱形天花板均涂有耐火隔热涂层。壳体包围平行于垂直轴的卡口式管,该垂直轴从壳体的底部一直延伸到拱形顶棚,反应流体在拱顶内流动。每个刺刀管沿烟管的整个长度围绕。每个刺刀管的入口和出口延伸到反应堆外部,超过拱形顶棚。热气在反应器外部产生,被引入具有较低底部开口的壳体内部,然后进入带有钻孔的烟管进入壁,并通过顶部和下方的排出口离开烟管。侧面开口。每个卡口管和烟管通过夹具系统从换热器反应器的拱形天花板上悬挂下来。每个卡口管之间的间距或中心到中心的距离是外管内径的2-5倍。每个烟管分为上陶瓷金属和下陶瓷金属。耐火砖拱用于覆盖热交换器反应器的整个部分,并位于火管的上下陶瓷金属部分之间的连接处,以允许烟管通过。密封板位于热交换器反应器管的顶部,并固定在烟管上。烟管安装在位于壳体水平面以下的开口下部,其上部装有位于密封板上方的排放孔。卡口管的密度为2-12管/ m 2>反应器的截面。密封板有很多折痕,以确保其自身的热膨胀。包括以下独立权利要求:(1)使用热交换器反应器蒸汽重整烃馏分的方法; (2)组装热交换器反应器的方法。

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