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    • 102. 发明授权
    • Processing hydrocarbon gases with selected physical solvents
    • 用选定的物理溶剂处理烃类气体
    • US4883515A
    • 1989-11-28
    • US102350
    • 1987-09-29
    • Yuv R. MehraFreylon B. Coffey
    • Yuv R. MehraFreylon B. Coffey
    • B01D53/14C01B3/52C01B21/04C07C7/11C10G5/04C10L3/10
    • C10L3/10B01D53/1487B01D53/1493C01B21/0488C01B3/52C07C7/11C10G5/04C01B2210/007C10G2300/1025
    • A continuous process is disclosed for separating components of a hydrocarbon gas stream which are selected from the group consisting of methane, ethane, higher saturated hydrocarbons, and mixtures thereof by countercurrently contacting the hydrocarbon gas stream with a physical solvent selected from the group consisting of:(1) paraffinic solvents having molecular weights ranging from 75 to 140 and UOP characterization factors ranging from 12.0 to 13.5, these factors being independent of the aromatic content of the paraffinic solvents,(2) naphthenic solvents having molecular weights ranging from 75 to 130 and UOP characterization factors ranging from 10.5 to 12.0, these factors being independent of the aromatic content of the naphthenic solvents, and(3) benzene and toluene,to produce an overhead stream which is rich in methane and a rich solvent bottoms stream and then recovering the lean physical solvent and a C.sub.2 + hydrocarbons product from the rich solvent bottoms stream and recycling the recovered solvent stream to the contacting step.
    • 公开了一种连续的方法,用于通过将烃气流与选自以下的物理溶剂逆流接触来分离选自甲烷,乙烷,较高级饱和烃及其混合物的烃气流的组分: (1)分子量范围为75至140,UOP表征因子范围为12.0至13.5的石蜡溶剂,这些因素与石蜡溶剂的芳族含量无关,(2)分子量范围为75至130的环烷烃溶剂和 UOP表征因子范围为10.5〜12.0,这些因素与环烷溶剂的芳香族含量无关,(3)苯和甲苯,产生富含甲烷和富溶剂塔底物流的塔顶物流,然后回收 稀的物理溶剂和来自富溶剂底部物流和回收物的C2 +烃产物 将回收的溶剂流转移到接触步骤。