期刊文献+

层状非均质多孔介质中LNAPLs污染物运移与分布的锋面扩展模型 被引量:3

Infiltration & Distribution front Spreading Model of LNAPLs in Layered Heterogenious Porous Media
在线阅读 下载PDF
导出
摘要 通过建立二维物理模型,研究非饱和层状非均质多孔介质中轻非水相液体LNAPLs(Light Non-a-queous Phase Liquids)的入渗机制与变化特征,建立LNAPLs运移与分布的锋面扩展模型,探讨入渗阶段油流锋面扩展速率的变化规律。结果发现:模型中砂土的渗透系数、孔隙度及油的相对渗透系数对LNAPLs运移的锋面扩展速率影响较大,而油的饱和度与压头变化对其影响较小。当LNAPLs由中砂进入细砂与细砂倾斜透镜体时,砂的渗透系数、孔隙度及油的相对渗透系数减小,这种介质结构面的突变改变了LNAPLs锋面扩展速率,其在中砂中锋面扩展速率快而在细砂与细砂倾斜透镜体中锋面扩展速率慢。此外,当LNAPLs进入干湿界面后,由于毛细作用的增强与含水量的加大,其横向比垂向运移的平均锋面扩展速率大。 The paper is based on a 2-D physical model,the purpose is to explore characteristics of LNAPLs infiltration in unsaturated layered heterogeneous porous media,and establish the inflitration and distribution of LNAPLs front spreading model,forecast the characteristic ratio of oil spreading rate in infiltration stage.The result show that capillary,porosity of sand and relative capillary of oil in model affect LNAPLs front spreading rate,but saturation of oil and the pressure head changed influence is small.When LNAPLs transfer from medium sand to fine,the capillary、porosity of sand and relative capillary of oil,this medium structure of mutation change LNAPLs frontal migration of rate,in the medium sand layered front spreading velocity is quickly and slow in the fine sand layered.In addition,when LNAPLs get to the dry and wet interface,for the capillary of pore water is stronger.
出处 《地下水》 2012年第3期106-109,共4页 Ground water
基金 广西自然科学基金(No.2011GXNSFB018004) 广西环境工程与保护评价重点实验室研究基金(No.桂科能0801Z007) 桂林理工大学博士基金(No.002401003254)
关键词 轻非水相液体 锋面扩展模型 多孔介质 运移与分布 毛细作用 Non-aqueous phase liquids front spreading model porous media infiltration and distribution
  • 相关文献

参考文献12

二级参考文献27

  • 1郑冰,陈家军,尉斌,支银芳.多孔介质不溶混流体毛细压力与饱和度关系实验研究[J].水动力学研究与进展(A辑),2005,20(5):665-672. 被引量:7
  • 2Illangasekare T H,Ramsey J L,Karsten H J,Michael B B.ExperimentalStudy of Movement and Distribution of Dense Organic Contaminants in Heterogeneous Aaquifers[J].Journal of Contaminant Hydrology,1995,20:1-25.
  • 3Abriola L M,Pinder G F.A multiphase approach to the modeling of porous media contamination by organic compounds,1.Equation development[J].Water Resour.Res.,1985,21(1):11-18.
  • 4Faust C R,Guswa J H,Mercer J W.Simulation of three-dimensional flow of immiscible fluids within and below the unsaturated zone[J].Water Resour.Res.,1989,25(12):2449-2464.
  • 5Kaluarachi J J,Parker J C.An efficient finite element method for modelingof multiphase flow[J].Water Resour.Res.,1989,25(10):43-54.
  • 6Kueper B H,Frind E O.Two-phase flow in heterogeneous porous media.1.Model development[J].Water Resour.Res.,1991,27(6):1049-1057.
  • 7Adenekan A E,Patzek T W,Pruess K.Modeling of multiphase transport of multicomponent organic contaminants and heat in the subsurface:Numerical Model Formulation[J].Water Resour.Res.,1993,29(11):3727-3740.
  • 8Moridis G.,Pruess K.Flow and transport simulation using T2CG1,A package of conjugate gradient solvers for the TOUGH2 family of codes[R].Technaical Report,LBL-36235.
  • 9Schwille F.Dense chlorinated solvents in porous and fractured media[M].Lewis,Chelsea.MI.1988.
  • 10Compbell J H.Nonaqueous phase liquid flow through porous media:experimental study and conceptual sharp-front model development[J].M.S.Thesis,Department of Civil Environemntal and Architectural Eng.,University of Colorado,Boulder,CO,1992,179.

共引文献90

同被引文献77

引证文献3

二级引证文献20

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部