首页> 外国专利> Device for separating normal-paraffinic hydrocarbons/olefinic hydrocarbons from fraction comprising hydrocarbons by adsorption in simulated mobile bed, comprises column having adsorbent beds separated by distributor/extractor plates

Device for separating normal-paraffinic hydrocarbons/olefinic hydrocarbons from fraction comprising hydrocarbons by adsorption in simulated mobile bed, comprises column having adsorbent beds separated by distributor/extractor plates

机译:在模拟移动床中通过吸附从含烃馏分中分离正链烷烃/烯烃的装置,该装置包括具有吸附剂床的塔,吸附剂床由分配器/萃取器板隔开

摘要

The device for separating normal-paraffinic hydrocarbons/olefinic hydrocarbons from a fraction comprising hydrocarbons by adsorption in simulated mobile bed, comprises a column having adsorbent beds (A i) separated by distributor/extractor plates (P i) for sequential feeding and extracting of two feeding fluids, a charge F, a desorbent D, two drawing fluids, a raffinate R and an extract E, a F-Net network of charge, D-Net network of adsorbent, a R-Net network of raffinate and E-Net network of extract, each of the networks are connected to the column by lines. The device for separating normal-paraffinic hydrocarbons/olefinic hydrocarbons from a fraction comprising hydrocarbons by adsorption in simulated mobile bed, comprises a column having adsorbent beds (A i) separated by distributor/extractor plates (P i) for sequential feeding and extracting of two feeding fluids, a charge F, a desorbent D, two drawing fluids, a raffinate R and an extract E, a F-Net network of charge, D-Net network of adsorbent, a R-Net network of raffinate and E-Net network of extract, each of the networks are connected to the column by lines comprising sectioning valves controlled in two-ways with aperture diameter greater than or equal to alpha value called network valves. The distributor/extractor plates are laid between the adsorbent beds. Each distributors/extractor plates of each of the areas are with single common network for feeding and withdrawing of networks. The plates (P i, P i + 1) of each section (S k) are connected between each other by a line of main external derivation (L k) connected with each of plates of the section by a nozzle comprising a sectional valve controlled in two-ways having plates (P i or P i + 1) called plate valve (V i or V i + 1). Each of the bypass lines comprises a control unit for limiting the circulating flow in main external derivation, which is either installed on the line of main external derivation or a bypass around the plate valve. The bypass of each section is linked to each of the networks via a single line of internal diameter higher or equal to a valve of a single network, respectively V-Fk, V-Dk, V-Rk, V-Ek with an opening diameter greater than or equal to alpha. Secondary external bypass lines (M k) connecting two adjacent sectors (S k - 1 and S k) through two connecting points. The first connecting point is laid on the nozzle connected to the lower plate (P i - 1) of the upper sector (S k - 1) between P i - 1 and the plate valves (V i - 1). The second connecting point is laid on the nozzle connected to top plate (P i) of the lower sector (S k) between P i and the plate valve (V i). Each external secondary bypass (M k) comprises a valve controlled in two-ways V-Mk of internal opening diameter of = 0.6 alpha. The line of derivation has a diameter less than or equal to the largest opening diameter of network valves linked to the main external derivation. The entire column is made by the superimposed adjacent sections except for the head plate. The column comprises a lower output line similar to a plate corresponding to lower adsorbent bed. The unit limiting the circulating flow comprises a controlled valve of opening diameter less than or equal to beta. Each of the secondary bypass lines comprises a control unit. A sequential feeding network RE-Net of a fluid of reflux RE comprises the extract, where the network is connected to each sector through a single internal diameter greater than or equal to alpha comprising to a single network valve (V-REk), which has an opening diameter greater than or equal to alpha. A sequential withdrawing network R2-Net of a second raffinate is connected to each sector through a single line of internal diameter greater than or equal to alpha comprising a single valve network (V-R2k), which has an opening diameter greater than or equal to alpha. An independent claim is included for a method for separating a product using the device.
机译:用于通过在模拟移动床中吸附从含烃馏分中分离正链烷烃/烯烃的装置,该装置包括具有吸附剂床(A i)的塔,吸附剂床由分配器/萃取器板(P i)隔开,用于依次进料和萃取两种进料液,装料F,解吸剂D,两种抽提液,提余液R和萃取液E,F-Net装料网络,D-Net吸附剂网络,R-提余液R-Net网络和E-Net网络提取后,每个网络都通过线连接到列。用于通过在模拟移动床中吸附从含烃馏分中分离正链烷烃/烯烃的装置,该装置包括具有吸附剂床(A i)的塔,吸附剂床由分配器/萃取器板(P i)隔开,用于依次进料和萃取两种进料液,装料F,解吸剂D,两种抽提液,提余液R和萃取液E,F-Net装料网络,D-Net吸附剂网络,R-提余液R-Net网络和E-Net网络对于萃取物,每个网络都通过管线连接到色谱柱,该管线包括以双向控制的,具有孔径大于或等于alpha值的分段阀,称为网络阀。分配器/提取器板放置在吸附剂床之间。每个区域的每个分配器/提取器板都具有用于馈送和撤回网络的单个公共网络。每个部分(S k)的板(P i,P i +1)通过一条主外导线(L k)相互连接,该主外部导数(L k)通过一个喷嘴控制,该喷嘴包括一个可控的分段阀在具有板(P i或P i + 1)的两通阀中称为板阀(V i或V i +1)。每个旁通管线包括用于限制主外部导数中的循环流量的控制单元,该控制单元安装在主外部导数线上或围绕板式阀的旁路。每个部分的旁路通过一条内径大于或等于单个网络阀的单线连接到每个网络,分别具有开口直径的V-Fk,V-Dk,V-Rk,V-Ek大于或等于alpha。通过两个连接点连接两个相邻扇区(S k-1和S k)的次级外部旁路管线(M k)。第一连接点位于喷嘴上,该喷嘴连接到P i-1和板阀(V i-1)之间的上扇形区(S k-1)的下板(P i-1)。第二连接点位于喷嘴上,该喷嘴连接到P i和板阀(V i)之间的下部扇形(S k)的顶板(P i)。每个外部次级旁路(M k)都包括一个阀,该阀以内部开口直径= 0.6 alpha的双向V-Mk控制。派生线的直径小于或等于链接到主要外部派生的网络阀的最大开口直径。整个立柱由顶板以外的相邻相邻部分组成。该塔包括类似于对应于下部吸附剂床的板的下部输出管线。限制循环流量的单元包括一个开口直径小于或等于β的受控阀。每个次级旁路管线包括控制单元。回流液RE的顺序进料网络RE-Net包含提取物,其中网络通过大于或等于alpha的单个内径连接到每个扇区,包括单个网络阀(V-REk),开口直径大于或等于alpha。第二萃余液的顺序抽取网络R2-Net通过内径大于或等于alpha的单线连接到每个扇区,该单线包括单个阀网(V-R2k),其开口直径大于或等于α。包括关于使用该设备分离产品的方法的独立权利要求。

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