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  • GEOMAR Catalogue / E-Books  (1)
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  • 1
    Online Resource
    Online Resource
    Boca Raton :CRC Press LLC,
    Keywords: Electronic books.
    Type of Medium: Online Resource
    Pages: 1 online resource (573 pages)
    Edition: 2nd ed.
    ISBN: 9781351463379
    DDC: 536.2
    Language: English
    Note: Cover -- Half Title -- Title Page -- Copyright Page -- Dedication -- Table of Contents -- Preface -- Preface to the First Edition -- Symbols -- Unit Conversions -- 1: INTRODUCTION -- 1.1 Regimes of boiling -- 1.2 Two-Phase Flow -- 1.3 Flow Boiling Crisis -- 1.4 Flow Instability -- 2: POOL BOlLING -- 2.1 Introduction -- 2.2 Nucleation and Dynamics of Single Bubbles -- 2.2.1 Nucleation -- 2.2.1.1 Nucleation in a Pure Liquid -- 2.2.1.2 Nucleation at Surfaces -- 2.2.2 Waiting Period -- 2.2.3 Isothermal Bubble Dynamics -- 2.2.4 Isobaric Bubble Dynamics -- 2.2.5 Bubble Departure from a Heated Surface -- 2.2.5.1 Bubble Size at Departure -- 2.2.5.2 Departure Frequency -- 2.2.5.3 Boiling Sound -- 2.2.5.4 Latent Heat Transport and Microconvection by Departing Bubbles -- 2.2.5.5 Evaporation-of-Microlayer Theory -- 2.3 Hydrodynamics of Pool Boiling Process -- 2.3.1 The Helmholtz Instability -- 2.3.2 The Taylor Instability -- 2.4 Pool Boiling Heat Transfer -- 2.4.1 Dimensional Analysis -- 2.4.1.1 Commonly Used Nondimensional Groups -- 2.4.1.2 Boiling Models -- 2.4.2 Correlation of Nucleate Boiling Data -- 2.4.2.1 Nucleate Pool Boiling of Ordinary Liquids -- 2.4.2.2 Nucleate Pool Boiling with Liquid Metals -- 2.4.3 Pool Boiling Crisis -- 2.4.3.1 Pool Boiling Crisis in Ordinary Liquids -- 2.4.3.2 Boiling Crisis with Liquid Metals -- 2.4.4 Film Boiling in a Pool -- 2.4.4.1 Film Boiling in Ordinary Liquids -- 2.4.4.2 Film Boiling in Liquid Metals -- 2.5 Additional References for Further Study -- 3: HYDRODYNAMICS OF TWO-PHASE FLOW -- 3.1 Introduction -- 3.2 Flow Patterns in Adiabatic and Diabatic Flows -- 3.2.1 Flow Patterns in Adiabatic Flow -- 3.2.2 Flow Pattern Transitions in Adiabatic Flow -- 3.2.2.1 Pattern Transition in Horizontal Adiabatic Flow -- 3.2.2.2 Pattern Transition in Vertical Adiabatic Flow -- 3.2.2.3 Adiabatic Flow in Rod Bundles. , 3.2.2.4 Liquid Metal-Gas Two-Phase Systems -- 3.2.3 Flow Patterns in Diabatic Flow -- 3.3 Void Fraction and Slip Ratio in Diabatic Flow -- 3.3.1 Void Fraction in Subcooled Boiling Flow -- 3.3.2 Void Fraction in Saturated Boiling Flow -- 3.3.3 Diabatic Liquid Metal-Gas Two-Phase Flow -- 3.3.4 Instrumentation -- 3.3.4.1 Void Distribution Measurement -- 3.3.4.2 Interfacial Area Measurement -- 3.3.4.3 Measurement of the Velocity of a Large Particle -- 3.3.4.4 Measurement of Liquid Film Thickness -- 3.4 Modeling of Two-Phase Flow -- 3.4.1 Homogeneous Model/Drift Flux Model -- 3.4.2 Separate-Phase Model (Two-Fluid Model) -- 3.4.3 Models for Flow Pattern Transition -- 3.4.4 Models for Bubbly Flow -- 3.4.5 Models for Slug Flow (Taite] and Barnea, 1990) -- 3.4.6 Models for Annular Flow -- 3.4.6.1 Falling Film Flow -- 3.4.6.2 Countercurrent Two-Phase Annular Flow -- 3.4.6.3 Inverted Annular and Dispersed Flow -- 3.4.7 Models for Stratified Flow (Horizontal Pipes) -- 3.4.8 Models for Transient Two-Phase Flow -- 3.4.8.1 Transient Two-Phase Flow in Horizontal Pipes -- 3.4.8.2 Transient Slug Flow -- 3.4.8.3 Transient Two-Phase Flow in Rod Bundles -- 3.5 Pressure Drop in Two-Phase Flow -- 3.5.1 Local Pressure Drop -- 3.5.2 Analytical Models for Pressure Drop Prediction -- 3.5.2.1 Bubbly Flow -- 3.5.2.2 Slug Flow -- 3.5.2.3 Annular Flow -- 3.5.2.4 Stratified Flow -- 3.5.3 Empirical Correlations -- 3.5.3.1 Bubbly Flow in Horizontal Pipes -- 3.5.3.2 Slug Flow -- 3.5.3.3 Annular Flow -- 3.5.3.4 Correlations for Liquid Metal and Other Fluid Systems -- 3.5.4 Pressure Drop in Rod Bundles -- 3.5.4.1 Steady Two-Phase Flow -- 3.5.4.2 Pressure Drop in Transient Flow -- 3.5.5 Pressure Drop in Flow Restriction -- 3.5.5.1 Steady-State, Two-Phase-Flow Pressure Drop -- 3.5.5.2 Transient Two-Phase-Flow Pressure Drop -- 3.6 Critical Flow and Unsteady Flow. , 3.6.1 Critical Flow in Long Pipes -- 3.6.2 Critical Flow in Short Pipes, Nozzles, and Orifices -- 3.6.3 Slowdown Experiments -- 3.6.3.1 Experiments with Tubes -- 3.6.3.2 Vessel Slowdown -- 3.6.4 Propagation of Pressure Pulses and Waves -- 3.6.4.1 Pressure Pulse Propagation -- 3.6.4.2 Sonic Wave Propagation -- 3.6.4.3 Relationship Among Critical Discharge Rate, Pressure Propagation Rate, and Sonic Velocity -- 3.7 Additional References for Further Study -- 4: FLOW BOILING -- 4.1 lntroducton -- 4.2 Nucleate Boiling in Flow -- 4.2.1 Subcooled Nucleate Flow Boiling -- 4.2.1.1 Partial Nucleate Flow Boiling -- 4.2.1.2 Fully Developed Nucleate Flow Boiling -- 4.2.2 Saturated Nucleate Flow Boiling -- 4.2.2.1 Saturated Nucleate Flow Boiling of Ordinary Liquids -- 4.2.2.2 Saturated Nucleate Flow Boiling of Liquid Metals -- 4.3 Forced-Convection Vaporization -- 4.3.1 Correlations for Forced-Convection Vaporization -- 4.3.2 Effect of Fouling Boiling Surface -- 4.3.3 Correlations for Liquid Metals -- 4.4 Film Boiling and Heat Transfer in Liquid-Deficient Regions -- 4.4.1 Partial Film Boiling (Transition Boiling) -- 4.4.2 Stable Film Boiling -- 4.4.2.1 Film Boiling in Rod Bundles -- 4.4.3 Mist Heat Transfer in Dispersed Flow -- 4.4.3.1 Dispersed Flow Model -- 4.4.3.2 Dryout Droplet Diameter Calculation -- 4.4.4.1 Blowdown Heat Transfer -- 4.4.4.2 Heat Transfer in Emergency Core Cooling Systems -- 4.4.4.3 Loss-of-Coolant Accident (LOCA) Analysis -- 4.4.4 Transient Cooling -- 4.4.5 Liquid-Metal Channel Voiding and Expulsion Models -- 4.5 Additional References for Further Study -- 5: FLOW BOILING CRISIS -- 5.1 Introduction -- 5.2 Physical Mechanisms of Flow Boiling Crisis in Visual Observations -- 5.2.1 Photographs of Flow Boiling Crisis -- 5.2.2 Evidence of Surface Dryout in Annular Flow -- 5.2.3 Summary of Observed Results. , 5.3 Microscopic Analysis of CHF Mechanisms -- 5.3.1 Liquid Core Convection and Boundary-Layer Effects -- 5.3.1.1 Liquid Core Temperature and Velocity Distribution Analysis -- 5.3.1.2 Boundary-Layer Separation and Reynolds Flux -- 5.3.1.3 Subcooled Core Liquid Exchange and Interface Condensation -- 5.3.2 Bubble-Layer Thermal Shielding Analysis -- 5.3.2.1 Critical Enthalpy in the Bubble Layer (Tong et a!., 1996a) -- 5.3.2.2 Interface Mixing -- 5.3.2.3 Mass and Energy Balance in the Bubble Layer -- 5.3.3 Liquid Droplet Entrainment and Deposition in High- Quality Flow -- 5.3.4 CHF Scaling Criteria and Correlations for Various Fluids -- 5.3.4.1 Scaling Criteria -- 5.3.4.2 CHF Correlations for Organic Coolants and Refrigerants -- 5.3.4.3 CHF Correlations for Liquid Metals -- 5.4 Parameter Effects on CHF in Experiments -- 5.4.1 Pressure Effects -- 5.4.2 Mass Flux Effects -- 5.4.2.1 Inverse Mass Flux Effects -- 5.4.2.2 Downward Flow Effects -- 5.4.3 Local Enthalpy Effects -- 5.4.4 CHF Table of p-G-X Effects -- 5.4.5 Channel Size and Cold Wall Effects -- 5.4.5.1 Channel Size Effect -- 5.4.5.2 Effect of Unheated Wall in Proximity to the CHF Point -- 5.4.5.3 Effect of Dissolved Gas and Volatile Additives -- 5.4.6 Channel Length and Inlet Enthalpy Effects and Orientation Effects -- 5.4.6.1 Channel Length and Inlet Enthalpy Effects -- 5.4.6.2 Critical Heat Flux in Horizontal Tubes -- 5.4.7 Local Flow Obstruction and Surface Property Effects -- 5.4.7.1 Flow Obstruction Effects -- 5.4.7.2 Effect of Surface Roughness -- 5.4.7.3 Wall Thermal Capacitance Effects -- 5.4.7.4 Effects of Ribs or Spacers -- 5.4.7.5 Hot-Patch Length Effects -- 5.4.7.6 Effects of Rod Bowing -- 5.4.7.7 Effects of Rod Spacing -- 5.4.7.8 Coolant Property (D,O and H,O) Effects on CHF -- 5.4.7.9 Effects of Nuclear Heating -- 5.4.8 Flow Instability Effects -- 5.4.9 Reactor Transient Effects. , 5.5 Operating Parameter Correlations for CHF Predictions in Reactor Design -- 5.5.1 W-3 CHF Correlation and THINC-Il Subchannel Codes -- 5.5.1.1 W-3 CHF Correlation -- 5.5.1.2 THINC [J Code Verification -- 5.5.2 B & -- W-2 CHF Correlation (Gellerstedt et al., 1969) -- 5.5.2.1 Correlation for Uniform Heat Flux -- 5.5.2.2 Correlation for Nonuniform Heat Flux -- 5.5.3 CE-1 CHF Correlation (C-E Report, 1975. 1976) -- 5.5.4 WSC-2 CHF Correlation and HAMBO Code -- 5.5.4.1 Bowring CHF Correlation for Uniform Heat Flux (Bowring. 1972) -- 5.5.4.2 WSC-2 Correlation and HAMBO Code Verification (Bowring. 1979) -- 5.5.5 Columbia CHF Correlation and Verification -- 5.5.5.1 CHF Correlation for Uniform Heat Flux -- 5.5.5.2 COBRA IIlC Verification (Reddy and Fighetti. 1983) -- 5.5.5.3 Russian Data Correlation of Ryzhov and Arkhipow ( 1985) -- 5.5.6 Cincinnati CHF Correlation and Modified Model -- 5.5.6.1 Cincinnati CHF Correlation and COBRA IllC Verification -- 5.5.6.2 An Improved CHF Model for Low-Quality Flow -- 5.5.7 A.R.S. CHF Correlation -- 5.5.7.1 CHF Correlation with Uniform Heating -- 5.5.7.2 Extension A.R.S. CHF Correlation to Nonuniform Heating -- 5.5.7.3 Comparison of A.R.S. Correlation with Experimental Data -- 5.5.8 Effects of Boiling Length: ClSE-1 and ClSE-3 CHF Correlations -- 5.5.8.1 ClSE-1 Correlation -- 5.5.8.2 ClSE-3 Correlation for Rod Bundles (Bertoletti et al., 1965) -- 5.5.9 GE Lower-Envelope CHF Correlation and ClSE-GE Correlation -- 5.5.9.1 G E Lower-Envelope CHF Correlation -- 5.5.9.2 GE Approximate Dryout Correlation (GE Report, 1975) -- 5.5.1 0 Whalley Dry out Predictions in a Round Tube (Whalley et al.. 1973) -- 5.5.11 Levy's Dryout Prediction with Entrainment Parameter -- 5.5.12 Recommendations on Evaluation of CHF Margin in Reactor Design -- 5.6 Additional References for Further Study -- 6: INSTABILITY OF TWO-PHASE FLOW. , 6.1 Introduction.
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  • 2
    Publication Date: 2021-07-01
    Description: (Ultra) high‐pressure (HP) rocks can be exhumed rapidly by subduction reversal or divergent plate motion. Recent studies show that subduction reversal can in particular occur in a divergent double subduction zone when the slab pull of one slab exceeds that of the other, shorter one, which then experiences a net upward pull. This recent hypothesis, first proposed for Triassic HP‐rocks exposed in the central Qiangtang mélange belt in central Tibet, can explain the exhumation of (ultra) HP rocks through upward slab movement. However, this model lacks the support of kinematic evidence. In this study, based on the recognition of multiple deformational phases, we analyze the kinematics of the HP‐bearing mélange in central Qiangtang. Based on new 40Ar‐39Ar geochronology data and those collected from the literature, we present a temporal framework for the new observations. We recognize a switch in sense of shear between the prograde (D1) and exhumation (D2‐3) paths. The change of shear sense reflects the reversal from downward to upward movement of the oceanic slab below. Early D2 represents the early exhumation stage that caused retrograde metamorphism from eclogite to blueschist facies. No magmatism occurred during this period. Continued exhumation from blueschist facies to greenschist facies resulted in D2‐D3 structures. Voluminous igneous activity occurred during this stage. We suggest that subduction reversal in a divergent double subduction zone can best explain the kinematic evolution and temporal framework above. This exhumation model may provide a new perspective on the exhumation mechanism for other HP rocks around the world.
    Description: Key Points: Central Qiangtang HP‐bearing mélange formed by short‐lived southward subduction in a divergent double subduction setting. Progressive inversed shearing exhumed HP rocks. Subduction reversal in a divergent double subduction zone can exhume HP rocks through direct slab movement.
    Description: China Geological Survey (CGS) http://dx.doi.org/10.13039/501100004613
    Keywords: 551.8 ; Tibetan Plateau ; South Qiangtang Terrane ; subduction reversal ; divergent double subduction zone ; exhumation ; high‐pressure rocks
    Type: article
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