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DESIGN THEORIES OF CRYSTALLIZERS AND THEIR INDUSTRIAL APPLICATION

机译:设计结晶器及其工业应用的理论

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Industrial crystallization is discussed on the unit operation of chemical industrial processes in future and prospected to become more important. Chemical engineers on industrial crystallization are expected to make optimum crystallizers designed to produce desired crystals. Design theories of industrial crystallizers are summarized and their industrial applications are discussed. And development of industrial crystallization processes is mentioned. A: design factor decided by production rate, product size, growth rate and suspension density in table 4 [m~3]; C.F.C.: characteristic factor for crystallization in table 4 [-]; C: concentration [kmol·kg~(-1)(H_2O) or kmol·m~(-3)] ; ΔC: supersaturation [kmol·kg~(-1)(H_2O) or kmol·m~(-3)]; f': secondary nucleation rate per unit surface area of a seed crystal [number/m~4sec]; f'(e): feed rate to, or removal rate of number of crystal of size "e" from a crystallization [number/sec,m~2]; g(e): number of crystal of size "e" suspended in a crystallizer [number,m]; kv: shape factor [-]; e: crystal size [m]; ew: dominant size [m]; M: molecular weigh [kg/kmol]; m: uniformity number on population basis [-]; n: uniformity number on weight basis [-]; P: production rate [g/s]; r: relative cumulative or weight of product crystal [-]
机译:在未来的化学工业过程的单位运行中讨论了产业结晶,并展示变得更加重要。预计工业结晶的化学工程师将使设计用于产生所需晶体的最佳结晶剂。总结了工业结晶器的设计理论,并讨论了其工业应用。提到了产业结晶过程的发展。 - 答:设计因素通过生产率,产品尺寸,增长率和悬浮密度决定[m〜3]; C.F.C.:表4中结晶的特征因子[ - ]; C:浓度[kmol·kg〜(-1)(h_2o)或kmol·m〜(-3)]; ΔC:过饱和[kmol·kg〜(-1)(h_2o)或kmol·m〜(-3)]; F':种子晶体单位表面积的次要成核速率[数量/ m〜4sec]; f'(e):从结晶的尺寸“e”晶体数量的进料速率或去除率[数量/ sec,m〜2]; g(e):悬浮在结晶器[数量,m]中悬挂的尺寸“e”的晶体数量; kv:形状因子[ - ]; E:水晶尺寸[m]; ew:主导大小[m]; M:分子称量[kg / kmol]; M:人口均匀号码[ - ]; n:重量均匀的统一号[ - ]; P:生产率[g / s]; R:产品晶体的相对累积或重量[ - ]

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