Fuel gas developments / editor, Donald L. Wise.

Includes bibliographical references and index.

Chapter 1 Producing Transportable Gas Condensation Has Two Drawbacks Two Alternatives Exist Meeting Sales-Gas Specifications Mast Gas Specifications Contain If HC Is More Valuable as a Liquid If HC s More Valuable as a Gas Maximizing Liquid Recovery Value of NGL components Ethane and Heavier HC Components (C) Can Be Liquefied "Crude Spiking" 142 142 142 142 142 142 142 EVI 144 Aboyourua bursaxad seo 145 Definitions of LPG and NGL Liquid recovery processes Any Cooling Will Induce Condensation and 146 146 19N PA Absorptior/Lean Oil Process General Considerations In Most Lean OI Plants Liquid Recovery Levels 147 147 148 148 sabejueapesa Mechanical Refrigeration Joule-Thomson (0-T) Expansions Cryogenic (Expansion Turbine) Plants Advantages Process selection If the NGL Content of the Feed Gas is Low For Gases Very Rich in NGL If the Inlet Gas Pressure s Very High Low Inlet Gas Pressure Very Low Gas Rates Large Flow Rates Remote Wells 151 151 ESI ESI 154 154 154 154 154 154 Fractionation Design considerations SI Appendis A Membrane/Amine Hybnd Grissik Gas Plant, Sumatra Indonesia Case Study Appendis B ludge Digby Gan Plant Hikes Production with Quick Slovent Change-Out Case Study 691, Index.