LEADER 01273nam0-2200337---450- 001 990008568440403321 005 20100625152853.0 010 $a90-5063-328-5 035 $a000856844 035 $aFED01000856844 035 $a(Aleph)000856844FED01 035 $a000856844 100 $a20071022d2002----km-y0itay50------ba 101 0 $aeng$afre$aita 102 $aNL 105 $ay-------001yy 200 1 $a<>transformation of economic life under the Roman Empire$eproceedings of the second workshop of the international network Impact of Empire (Roman Empire , c. 200 B.C. - A.D. 476) Nottingham, july 4-7, 2001$fedited by Lukas de Blois & John Rich 210 $aAmsterdam$cJ.C. Gieben$d2002 215 $aXXII, 266 p., 7 p. di tav.$cill.$d25 cm 225 1 $aImpact of empire (Roman empire)$v2 702 1$aWiedemann,$bThomas E. J.$f<1950-2001> 702 1$aRich,$bJohn 702 1$aBlois,$bLukas de 710 12$aWorkshop of the international network impact of empire$d<2. ;$f2001 ;$eNottingham>$0502619 801 0$aIT$bUNINA$gRICA$2UNIMARC 901 $aBK 912 $a990008568440403321 952 $aDirez. 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Carroll, Qi Li 210 1$aHoboken, New Jersey ;$aSalem, Massachusetts :$cScrivener Publishing :$cWiley,$d2014. 210 4$dİ2014 215 $a1 online resource (421 p.) 225 1 $aAdvances in Natural Gas Engineering 300 $aDescription based upon print version of record. 311 $a1-322-06125-4 311 $a1-118-93856-9 320 $aIncludes bibliographical references and index. 327 $aCover; Title Page; Copyright Page; Contents; Preface; Section 1: Data and Correlations; 1 Densities of Carbon Dioxide-Rich Mixtures Part I: Comparison with Pure CO2; 1.1 Introduction; 1.2 Density; 1.3 Literature Review; 1.3.1 CO2 + Methane; 1.3.2 CO2 + Nitrogen; 1.4 Calculations; 1.4.1 Kay's Rule; 1.4.2 Modified Kay's Rule; 1.4.3 Prausnitz-Gunn; 1.5 Discussion; 1.6 Conclusion; References; 2 Densities of Carbon Dioxide-Rich Mixtures Part II: Comparison with Thermodynamic Models; 2.1 Introduction; 2.2 Literature Review; 2.3 Calculations; 2.4 Lee Kesler; 2.5 Benedict-Webb- Rubin (BWR) 327 $a2.6 Peng-Robinson2.7 Soave-Redlich-Kwong; 2.8 AQUAlibrium; 2.9 Discussion; 2.10 Conclusion; References; 3 On Transferring New Constant Pressure Heat Capacity Computation Methods to Engineering Practice; 3.1 Introduction; 3.2 Materials and Methods; 3.3 Results and Discussion; 3.4 Conclusions; References; 4 Developing High Precision Heat Capacity Correlations for Solids, Liquids and Ideal Gases; 4.1 Introduction; 4.2 Databases and Methods; 4.3 Results and Discussion; 4.4 Conclusion; References; 5 Method for Generating Shale Gas Fluid Composition from Depleted Sample; 5.1 Introduction 327 $a5.2 Theory of Chemical Equilibrium Applied to Reservoir Fluids5.3 Reservoir Fluid Composition from a Non-Representative Sample; 5.3.1 Depleted Gas Condensate Samples; 5.3.2 Samples from Tight Reservoirs; 5.4 Numerical Examples; 5.4.1 Depleted Gas Condensate Samples; 5.4.2 Samples from Tight Reservoirs; 5.5 Discussion of the Results; 5.6 Conclusions; 5.7 Nomenclature; Greek letters; Sub and super indices; References; 6 Phase Equilibrium in the Systems Hydrogen Sulfide + Methanol and Carbon Dioxide + Methanol; 6.1 Introduction; 6.2 Literature Review; 6.2.1 Hydrogen Sulfide + Methanol 327 $a6.2.2 Carbon Dioxide + Methanol6.3 Modelling With Equations Of State; 6.4 Nomenclature; Greek; References; 7 Vapour-Liquid Equilibrium, Viscosity and Interfacial Tension Modelling of Aqueous Solutions of Ethylene Glycol or Triethylene Glycol in the Presence of Methane, Carbon Dioxide and Hydrogen Sulfide; 7.1 Introduction; 7.2 Results and Discussion; 7.2.1 Experimental; 7.2.2 Vapour Liquid Equilibrium and Phase Density Modeling; 7.2.3 Liquid-Phase Viscosity Modeling; 7.2.4 Interfacial Tension Modeling; 7.2.5 Commercial Software Comparison; 7.3 Conclusions; 7.4 Nomenclature 327 $a7.5 AcknowledgementReferences; Appendix 7.A; Section 2: Process Engineering; 8 Enhanced Gas Dehydration using Methanol Injection in an Acid Gas Compression System; 8.1 Introduction; 8.2 Methodology; 8.2.1 Modeling Software; 8.2.2 Simulation Setup; 8.3 CASE I: 100 % CO2; 8.3.1 How Much to Dehydrate; 8.3.2 Dehydration using Air Coolers; 8.3.3 Methanol injection for hydrate suppression; 8.3.4 Methanol Injection for Achieving 2:1 Water Content; 8.3.5 DexProTM for Achieving 2:1 Water Content; 8.4 CASE II: 50 Percent CO2, 50 Percent H2S; 8.4.1- How Much to Dehydrate? 327 $a8.4.2 Dehydration using Air Coolers 330 $a This is the fourth volume in a series of books focusing on natural gas engineering, focusing on two of the most important issues facing the industry today: disposal and enhanced recovery of natural gas. This volume includes information for both upstream and downstream operations, including chapters on shale, geological issues, chemical and thermodynamic models, and much more. Written by some of the most well-known and respected chemical and process engineers working with natural gas today, the chapters in this important volume represent the most cutting-edge and state-of-the-art processes 410 0$aAdvances in natural gas engineering. 606 $aOil wells$xGas lift 606 $aGas wells 606 $aCarbon dioxide$xIndustrial applications 606 $aGeological carbon sequestration 606 $aAtmospheric carbon dioxide$xStorage 615 0$aOil wells$xGas lift. 615 0$aGas wells. 615 0$aCarbon dioxide$xIndustrial applications. 615 0$aGeological carbon sequestration. 615 0$aAtmospheric carbon dioxide$xStorage. 676 $a622/.33827 702 $aWu$b Ying$c(Petroleum engineer), 702 $aCarroll$b John J.$f1958- 702 $aLi$b Qi$c(Geologist), 801 0$bMiAaPQ 801 1$bMiAaPQ 801 2$bMiAaPQ 906 $aBOOK 912 $a9910132344703321 996 $aGas injection for disposal and enhanced recovery$92137162 997 $aUNINA