7th edition. - USA: Campbell Petroleum Series, 1982. - 438 p. - на англ. яз.
This new Seventh Edition of "Gas Conditioning and Processing" has been edited to reflect continuing changes in our technology and the manner in which it is practiced. Most engineering calculations are performed on a computer and there often is little opportunity for the user to become very proficient in all areas for which he or she is responsible. The only practical answer is to understand the relatively few fundamentals which govern the multitude of applications for them.
============================================================
В третьем томе данной серии рассмотрены следующие разделы технологии подготовки и переработки природного газа: фазовые равновесия в углеводородных смесях, предикативные методы термодинамических свойств, расчеты фазового равновесия, свойства углеводородной фракции С
6+, усовершенствованные методы определения свойств, принципы непрерывной ректификации бинарных смесей, непрерывная ректификация многокомпонентных смесей, потарелочный метод расчета ректификации, абсорбция, гидравлический расчет колонного оборудования, процессы сжатия, процессы расширения, особенности взаимодействия смеси воды с природным газом, осушка, основы гидродинамики. В приложениях даны: коэффициенты пересчета из различных систем измерения, термодинамические данные.
"Garbage Begats garbage"
Phase Behavior of Hydrocarbon SystemsPure component phase behavior
Multicomponent phase behavior
Thermodynamic Property Prediction MethodsBasic thermodynamic property equations
Equation of state solution methods
Evaluation of thermodynamic property prediction procedures
Selecting a thermodynamic property prediction procedure
Equilibrium CalculationsBasic equilibrium calculations
Equilibrium calculation failures
Predicting the Properties of Hexanes Plus (C6+) FractionsC
6+ fraction availability
Advanced Characterization MethodsData requirements
Critical property estimation procedure
Verification of the method
Effect of proposed procedure on processing calculations
Principles of Continuous Binary DistillationMinimum trays
Minimum reflux
Complex fractionators
Continuous Multicomponent DistillationMinimum number of trays
Minimum reflux
Operating reflux and plates
Feed plate location
Influence of feed operation
Tray-By-Tray CalculationsLewis-Matheson method
Thiele-Geddes method
Contemporary tray-by-tray calculation procedures
Thermodynamic property prediction methods and C
6+ characterization Recommended procedure for distillation column simulation
"Diagnosing" tray-by-tray output
AbsorptionGraphical calculation
How an absorber operates
Multicomponent absorption
Stripping
Multicomponent stripping
Tray-by-tray calculations
Complex absorber calculations
Column Sizing CalculationsPlate (tray) towers
Effect of liquid hydraulics
CompressionPrediction methods
Mollier chart method
Gas law methods
True polytropic method
Efficiencies based on operating data
Comparison of the methods
Comparison of efficiencies
Corrections to the predicted gas power requirements
Optimum interstage pressures
Thermodynamic property prediction effects on compressor evaluation
Specific centrifugal compressor parameters
Second level efficiency estimation
Expansion ProcessesAdiabatic expansion processes
Cryogenic expander processing
Natural Gas–Water SystemPhase behavior
Water content prediction methods
Comparison of methods
Hydrate prediction
DehydrationAbsorber design factors
Regenerator design
Isotherms for molecular sieves
Fluid FlowGas flow equations
Two phase flow calculation methods: Lockhart-Martinelli, Baker, AGA, Flanigan, Beggs and Brill