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PACKING OF CROSS-CHANNEL STRUCTURE FOR MASS-TRANSFER PACKED COLUMN AT HIGH SPECIFIC CAPACITY OF SEPARATION AND METHOD OF OPERATION OF SUCH COLUMN
PACKING OF CROSS-CHANNEL STRUCTURE FOR MASS-TRANSFER PACKED COLUMN AT HIGH SPECIFIC CAPACITY OF SEPARATION AND METHOD OF OPERATION OF SUCH COLUMN
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机译：高比分离力的传质包装柱跨通道结构的堆积和这种柱的操作方法
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摘要
FIELD: mass- transfer checked columns. SUBSTANCE: specific surface of packing has angle ϕ of inclination of channels. It belongs to class (c1) at Ca = ac1 and ϕ = ϕc1 according to the following data: similar flows of liquids are preset for liquids flowing through packing; number "n" of theoretical stages of separation per meter is determined empirically, viz.: NTSM magnitude appears in form of first function f1(a,ϕ) of the variables "a" and ϕ; hydraulic resistance arising for gas flow running through packing is characterized by loss of pressure per meter, &Dgr;p as second function f2(a,ϕ); magnitude &Dgr;p has relative minimum at additional condition n=const when variable "a" and ϕ appear in form of magnitudes am(n) and ϕm(n) depending on magnitude "n"; conditions n 4,5 acl am(n), ϕc1 ϕm(n), as well as ϕc1 45° are true. EFFECT: enhanced economical efficiency of separation. 9 cl, 4 dwg
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机译：字段：传质检查的色谱柱。实质：填料的比表面有夹角φ。通道的倾斜度。它属于（c1）类，位于Ca = a c1 和＆phiv;处。 =＆phiv; c1 根据以下数据：对于流过填料的液体，预设了相似的液体流量;每米分离理论级数“ n”由经验确定，即：NTSM量级以变量“ a”和＆phiv的第一函数f 1 （a，phiv）的形式出现; ;流过填料的气流产生的水力阻力的特征在于每米压力损失，Δp是第二函数f 2 （a，phiv）;当变量“ a”和＆phiv; p在附加条件n = const时，幅度＆pgr具有相对最小值。取决于量级“ n”以量级a m （n）和＆phiv; m （n）的形式出现;条件n> 4,5 a cl m （n），＆phiv; c1 m （n）以及＆ltv; c1 ＆deg; 都是正确的。效果：提高了分离的经济效率。 9厘升，4载重吨
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