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级联过程理论研究与~(13)C浓缩

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作者. 级联过程理论研究与~(13)C浓缩[J]. 同位素, 1990, 3(4): 210-210. DOI: 10.7538/tws.1990.03.04.0210
引用本文: 作者. 级联过程理论研究与~(13)C浓缩[J]. 同位素, 1990, 3(4): 210-210. DOI: 10.7538/tws.1990.03.04.0210
THEORETICAL STUDY OF CASCADE PROCESS AND ENRICHMENT OF ~(13)C[J]. Journal of Isotopes, 1990, 3(4): 210-210. DOI: 10.7538/tws.1990.03.04.0210
Citation: THEORETICAL STUDY OF CASCADE PROCESS AND ENRICHMENT OF ~(13)C[J]. Journal of Isotopes, 1990, 3(4): 210-210. DOI: 10.7538/tws.1990.03.04.0210

级联过程理论研究与~(13)C浓缩

THEORETICAL STUDY OF CASCADE PROCESS AND ENRICHMENT OF ~(13)C

  • 摘要: 建造了—座2-7型不锈钢试验——生产装置,以天然CO_2为原料,采用CO_2-二正丁胺-三乙胺化学交换法浓缩高浓~(13)C;建立了多级梯型级联过程数学模型,关联了过程分离系数α、原利浓度xf、各塔流量L、塔径D、塔高H、填料当量直径D′_c等变量与应变量产率P、产品浓度xp之间的函数关系。该级联装置在产率为100g~(13)C/a出料过程中(150d)~(13)CO_2产品中~(13)C浓度保持在93%以上,最高达99.288%。
    Abstract: A pilot plant of Type 2-7 stainless steel cascade enriching highly concentrated ~(13)C using CO_2-di-n-butylamine-triethylamine chemical exchange system was set up; The mathematical model of the multistage trapezoid cascade was established, which describes the function relation among separation factor a, concentration of raw material x_i, flow of each column L, diameter of column D, height of column H, equivalent diameter ofpacking D_e, productive rate of cascade P and concentration of products x_p The cascade was run, and the concentrative rate of the cascade was sped up and the separative capacity of the cascade was fully developed. The concentrationof ~(13)CO_2-products remained more than 93 atom % and up to 99.288 atom % during 150 days of drawing-off of products at 100g ~(13)C/a.
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    [3] 杨国华、曾权兴,稳定同位素分离.北京,原子能出版社,1989年,P216.
    [4] Ghate, M. R. et al., Annual Progress Report COO-3263-3(1973).
    [5] Ghate., M. R. et al., Separation Science 10(5), 547(1975).
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出版历程
  • 收稿日期:  1990-06-28
  • 刊出日期:  1990-11-19

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