首页> 外国专利> PLANT FOR PHASE-SELECTIVE ADSORPTION OR ION EXCHANGE OF COMPONENT FROM DISPERSED FLUID OR LIQUID MEDIUM AND METHOD OF PHASE-SELECTIVE ADSORPTION OR ION EXCHANGE OF COMPONENT FROM DISPERSED FLUID OR LIQUID MEDIUM

PLANT FOR PHASE-SELECTIVE ADSORPTION OR ION EXCHANGE OF COMPONENT FROM DISPERSED FLUID OR LIQUID MEDIUM AND METHOD OF PHASE-SELECTIVE ADSORPTION OR ION EXCHANGE OF COMPONENT FROM DISPERSED FLUID OR LIQUID MEDIUM

机译:用于从分散的流体或液体介质中进行相选择吸附或离子交换的植物以及用于从分散的流体或液体介质中进行相选择吸附或离子交换的方法

摘要

FIELD: technology of adsorption and ion exchange processes for extraction and separation of components of dispersed and liquid media.;SUBSTANCE: proposed plant includes mixing reactor, displacement apparatus, two-section mass exchanger and pulsating system interconnected into suspension sorbent circulating loop. Sections of mass exchanger are made in form of extended passages divided by convectively permeable partition. Pulsating system forms alternating drops of pressure in passages. One passage of mass exchanger is connected to loop and other passage is connected to line of counter-flow delivery of medium to be treated. Loop is connected with fresh sorbent source and with used sorbent receiver. Line of medium to be treated is connected with carrying fluid source and receiver. Sections of mass exchanger may be of shell-and-tube type or of contact-plate type. Specification describes methods of phase-selective adsorption or ion exchange. Fresh sorbent is kept in source and is introduced into loop in form of concentrated fluid suspension in carrying preserving liquid. Waste sorbent is discharged from loop also in form of concentrated suspension. Size of dispersed particles of adsorbents, ionites and media being treated range from 0.3 to 0.7 mm. Adsorption or ion exchange processes are carried out in cyclic, continuous cyclic and fully continuous modes. As a result, productivity by component being extracted is increased by 5-10 times.;EFFECT: increased productivity; reduced number of production processes and equipment units.;23 cl, 3 dwg, 1 tbl, 21 ex
机译:领域:吸附和离子交换工艺,用于分离和分离分散介质和液体介质的组分。物质:拟建的工厂包括混合反应器,置换装置,两段式质量交换器和与悬浮液吸附剂循环回路互连的脉冲系统。质量交换器的部分以延伸通道的形式制成,该通道被对流可渗透的隔板隔开。脉动系统在通道中形成交替的压力降。质量交换器的一个通道连接到回路,另一通道连接到待处理介质的逆流输送管线。回路与新鲜的吸附剂源和用过的吸附剂接收器相连。待处理介质管线与输送流体源和接收器相连。质量交换器的部分可以是壳管式或接触板式的。规范描述了相选择吸附或离子交换的方法。新鲜的吸附剂被保留在源中,并以浓缩流体悬浮液的形式引入回路,以携带防腐液。废吸附剂也以浓缩悬浮液的形式从回路中排出。被处理的吸附剂,离子矿和介质的分散颗粒尺寸为0.3到0.7毫米。吸附或离子交换过程以循环,连续循环和完全连续模式进行。结果,提取出的组分的生产率提高了5-10倍。减少了生产流程和设备单元的数量。; 23 cl,3 dwg,1 tbl,21 ex

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