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裂隙介質污染物傳質動力學(英文版)

包郵 裂隙介質污染物傳質動力學(英文版)

出版社:科學出版社出版時間:2022-09-01
開本: 其他 頁數: 224
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裂隙介質污染物傳質動力學(英文版) 版權信息

  • ISBN:9787030729514
  • 條形碼:9787030729514 ; 978-7-03-072951-4
  • 裝幀:一般膠版紙
  • 冊數:暫無
  • 重量:暫無
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裂隙介質污染物傳質動力學(英文版) 內容簡介

本書吸收了裂隙介質污染物傳質動力學國內外近期新研究成果,從培養高層次創性人才知識結構需求出發,注重內容的理論性、系統性、前沿性和完整性;谙到y的概念,論述了裂隙介質的概念、結構與性質;裂隙介質滲流的基本定律;裂隙介質的基本傳質理論;裂隙介質傳質過程的數值模擬;裂隙介質傳質的數學模型與參數反演;裂隙介質傳質前沿問題等。

裂隙介質污染物傳質動力學(英文版) 目錄

Contents
Preface
Chapter 1 Introduction 1
1.1 Mass transfer in saturated system 4
1.2 Mass transfer in unsaturated system 11
Chapter 2 Concepts, Structure, and Properties of Fractured Media 15
2.1 Basic concepts of fractured media 15
2.2 Structure of fractured media 19
2.3 Properties of fractured media 23
2.3.1 Porosity of rock mass 23
2.3.2 Permeability of rock mass 24
2.3.3 Permeability of geologic formations 27
2.4 Characterization and reconstruction of fractured media 30
2.4.1 2D self-affine fracture generation 30
2.4.2 3D sheared fractures with the shear displacement 35
Chapter 3 Basic Law of Fluid Flow in Fractured Media 38
3.1 Basic concepts of fluid flow in fractured media 38
3.1.1 Viscous versus inviscid regions of flow 39
3.1.2 Laminar versus turbulent flow 39
3.1.3 One-, two-, and three-dimensional flows 40
3.2 Linear flow law 41
3.2.1 Darcy’s Law 41
3.2.2 Cubic law 45
3.3 Non-linear flow law 49
3.3.1 Izbash equation 50
3.3.2 Forchheimer equation 50
3.4 Multiphase flow 52
3.4.1 Basic concept of multiphase flow 52
3.4.2 Immiscible fluid flow 62
3.4.3 Immiscible three-phase flow 63
Chapter 4 Basic Process of Mass Transfer in Fractured Media 65
4.1 Diffusion 65
4.2 Brownian motion and Fick’s Law 70
4.2.1 Brownian motion 70
4.2.2 Fick’s First Law 74
4.2.3 Fick’s Second Law 75
4.3 Advection 77
4.4 Difference in dispersion and diffusion 79
4.5 Taylor dispersion 84
4.6 Adsorption and desorption 90
4.7 Precipitation and dissolution 91
Chapter 5 Mathematical Model of Mass Transfer in Fractured Media 93
5.1 Analytical solution of advection-dispersion equation (ADE) model 93
5.1.1 ADE model and analytical solution in one-dimensional fractured media 93
5.1.2 ADE model and analytical solution in two-dimensional fractured media 94
5.1.3 ADE model and analytical solution in three-dimensional fractured media 102
5.2 Continuous time random walk (CTRW) model 106
5.3 Mobile-Immobile (MIM) model 107
5.4 Spatial moment 108
5.5 Scalar dissipation rate(SDR)and dilution index 110
5.5.1 Scalar dissipation rate (SDR) 110
5.5.2 Dilution index 112
Chapter 6 Numerical Methods of Mass Transfer Process in Fractured Media 114
6.1 Lattice Boltzmann method 114
6.2 Immiscible two-phase transport model: Phase field method 119
6.3 Pore-scale aqueous solute transport model 121
6.4 Coupling strategy 122
6.5 Behaviors of aqueous tracer mass transfer 125
Chapter 7 Mass Transfer Between Matrix and Filled Fracture During Imbibition Process 134
7.1 LF-NMR measurement and principle 134
7.2 Experimental materials 136
7.3 Distribution of the imbibed water 138
7.4 Imbibition rate and analytical model 143
Chapter 8 Influence of Wettability on Interfacial Area for Immiscible Liquid Invasion 149
8.1 Interfacial area for immiscible liquid invasion 149
8.2 Entry pressure 151
8.3 Two phase flow characteristics 153
8.4 Capillary pressure saturation and interfacial area relationships 156
Chapter 9 Multiscale Roughness Influence on Solute Transport in Fracture 162
9.1 Statistical self-affine property 162
9.2 Roughness decomposition 166
9.3 Flow field characteristics in fractures 171
9.4 Relationship between tracer longitudinal dispersion and Peclet number 172
Chapter 10 Influence of Eddies on Solute Transport Through a Fracture 180
10.1 Flow field and eddies formation 180
10.2 Spatial evolution of solute and BTC characteristics 183
10.3 Inverse model for non-Fickian BTCs 187
10.4 Uniformity of concentration distribution 189
Chapter 11 Lattice Boltzmann Simulation of Solute Transport in Fractures 192
11.1 Coupling flow and concentration fields based on LBM 192
11.2 Taylor dispersion simulation based on LBM 194
11.3 Characteristics of solute transport in a single rough fracture 195
References 201
List of Frequently Used Symbols 213
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裂隙介質污染物傳質動力學(英文版) 節選

Chapter 1 Introduction NAPL (Non-aqueous Phase Liquid) is a typical subsurface organic pollutant, such as tetrachloroethylene, trichloroethylene, and methylbenzene. Although the solubility of NAPLs in water is quite low (for example, the solubility of tetrachloroe- thylene in water is only 0.015 g/100 mL), their harmfulness to the groundwater environment is surprising. Many NAPLs pose a high risk of cancer. The World Health Organization’s drinking water standard requires that benzene and trichloroethylene contain no more than 0.005 mg per liter of water, and vinyl chloride, which poses a higher cancer risk, must contain no more than 0.002 mg per liter of water. Although the solubility of many NAPLs in groundwater is quite low, it is still above the safety standard for drinking water. NAPLs are divided by the density of pure water. One is heavier than water and is referred to as DNAPL (dense NAPL), while another is lighter than water and is referred to as LNAPL (light NAPL). Compared to LNAPL, DNAPL has a higher density than water and sinks continuously after entering the groundwater. DNAPL has the characteristics of concealment and persistence, and the problems of migration and mass transfer in fractured groundwater are more complex. DNAPL is a very special organic pollutant. Its migration and mass transfer process has the characteristics of soluble and insoluble pollutants. This is mainly because most liquid DNAPL cannot be completely dissolved in a short time and discharged from the subsurface with the runoff, but remain in the frac medium for a long time in the form of a “DNAPL pollution pool” that slowly dissolves and expands its plume with the runoff from the subsurface. The process of DNAPL migrating with the water flow as a liquid in a non-aqueous phase and DNAPL migrating with the water flow after being dissolved by the water is referred to here as mass transfer. The mass transfer process of DNAPL in fractured groundwater consists of the migration of an immiscible two-phase flow and the migration of solutes after the DNAPL is dissolved. The mass transfer of contaminant in fractured media plays an important role in the surface environment problems (e.g., contaminant degradation (Sale et al., 2008), nuclear waste disposal (Bagalkot and Kumar, 2016), and bioremediation (Song et al., 2014). In recent decades, the investigation of dilution and mixing processes in fractured media has been focused by the scholars in various fields (Anna et al., 2014; Soltanian et al., 2015; Dou et al., 2018a; Dou et al., 2018b). The characterization of the spreading and mixing processes of the conservative solute is instrumental in understanding and assessing reactive solute transport, which is necessary for studying complex chemical biological reaction transport in groundwater. Although many studies (Shapiro and Brenner, 1988; Pini et al., 2016) have provided new insights into the mechanisms and properties of the mixing behavior at the Darcy scale or the larger field scale, little attentions have been focused on porous media at the pore scale. There is always an influence of the smaller-scale processes on the larger scale behaviors (Bear, 2013). Therefore, to understand and evaluate mixing processes at pore-scale with suitable methods is very significant (Rolle et al., 2013). The migration process of DNAPL in fractured groundwater can be divided into three stages: The first stage is the overall intrusion stage of DNAPL; the second stage is the comigration stage of DNAPL and water flow; the third stage is the residual dissolution stage of DNAPL, as shown in Figure 1.1.1. The residual DNAPL of fractured groundwater refers to the DNAPL that cannot be displaced by water flow alone under the conditions of natural water flow and pressure. Since the dissolution rate of DNAPL is affected by its interface area, hydrodynamic conditions, and geometric characteristics of fractures, its dissolution content in water can be ignored compared to the penetration of DNAPL in a short time. Generally, the migration process of DNAPL in the first and second stages is considered only as two-phase immiscible flow migration process, while the solubility of DNAPL in water is ignored. In the third stage, the remaining DNAPL is relatively stable and no longer migrates as a whole, but continuously dissolves in the water body and increases its dissolved pollution plume by the effect of groundwater discharge. In this stage, the problem of DNAPL dissolution process and solute transport with DNAPL as solute must be considered. The first and second stages directly affect the distribution characteristics of DNAPL residues in fractured media in the third stage, and the third stage is an important reason for the persistence and concealment of DNAPL pollutants. The spatial heterogeneities of the pore space in aquifers lead to the complex fluid flow and anomalous solute transport. As the occurrence of preferential flow paths and/o

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