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Contributors | ||
Preface | ||
Acknowledgements | ||
Licensing Contracts | ||
Pt. 1 | Alkylation and Polymerization | |
Ch. 1.1 | NExOCTANE Technology for Isooctane Production | |
Ch. 1.2 | STRATCO Effluent Refrigerated H[subscript 2]SO[subscript 4] Alkylation Process | |
Ch. 1.3 | UOP Alkylene Process for Motor Fuel Alkyation | |
Ch. 1.4 | UOP HF Alkylation Technology | |
Ch. 1.5 | Linear Alkylbenzene (LAB) Manufacture | |
Ch. 1.6 | Q-Max Process for Cumene Production | |
Ch. 1.7 | ConocoPhillips Reduced Volatility Alkylation Process (ReVAP) | |
Pt. 2 | Base Aromatics Production Processes | |
Ch. 2.1 | Aromatics Complexes | |
Ch. 2.2 | UOP Sulfolane Process | |
Ch. 2.3 | UOP Thermal Hydrodealkylation (THDA) Process | |
Ch. 2.4 | BP-UOP Cyclar Process | |
Ch. 2.5 | UOP Isomar Process | |
Ch. 2.6 | UOP Parex Process | |
Ch. 2.7 | UOP Tatoray Process | |
Pt. 3 | Catalytic Cracking | |
Ch. 3.1 | KBR Fluid Catalytic Cracking Process | |
Ch. 3.2 | Deep Catalytic Cracking, the New Light Olefin Generator | |
Ch. 3.3 | UOP Fluid Catalytic Cracking Process | |
Ch. 3.4 | Stone & Webster - Institut Francais du Petrole Fluid RFCC Process | |
Pt. 4 | Catalytic Reforming | |
Ch. 4.1 | UOP Platforming Process | |
Pt. 5 | Dehydrogenation | |
Ch. 5.1 | UOP Oleflex Process for Light Olefin Production | |
Ch. 5.2 | UOP Pacol Dehydrogenation Process | |
Pt. 6 | Hydrogen Production | |
Ch. 6.1 | FW Hydrogen Production | |
Pt. 7 | Hydrocracking | |
Ch. 7.1 | Isocaracking - Hydrocracking for Superior Fuels and Lubes Production | |
Ch. 7.2 | UOP Unicracking Process for Hydrocracking | |
Pt. 8 | Hydrotreating | |
Ch. 8.1 | Chevron Lummus Global RDS/VRDS Hydrotreating - Transportation Fuels from the Bottom of the Barrel | |
Ch. 8.2 | Selective Hydrogenation Processes | |
Ch. 8.3 | UOP Unionfining Technology | |
Ch. 8.4 | UOP RCD Unionfining Process | |
Ch. 8.5 | UOP Catalytic Dewaxing Process | |
Ch. 8.6 | UOP Unisar Process for Saturation of Aromatics | |
Ch. 8.7 | Chevron Lummus Global Ebullated Bed Bottom-of-the-Barrel Hydroconversion (LC-Fining) Process | |
Pt. 9 | Isomerization | |
Ch. 9.1 | UOP Bensat Process | |
Ch. 9.2 | UOP Butamer Process | |
Ch. 9.3 | UOP Penex Process | |
Ch. 9.4 | UOP TIP and Once-Through Zeolitic Isomerization Processes | |
Ch. 9.5 | UOP Par-Isom Process | |
Pt. 10 | Separation Processes | |
Ch. 10.1 | Chevron Lummus Global On-Stream Catalyst Replacement Technology for Processing High-Metal Feeds | |
Ch. 10.2 | The ROSE Process | |
Ch. 10.3 | UOP Sorbex Family of Technologies | |
Ch. 10.4 | UOP/FW USA Solvent Deasphalting Process | |
Ch. 10.5 | UOP IsoSiv Process | |
Ch. 10.6 | Kerosene IsoSiv Process for Production of Normal Paraffins | |
Ch. 10.7 | UOP Molex Process for Production of Normal Paraffins | |
Ch. 10.8 | UOP Olex Process for Olefin Recovery | |
Pt. 11 | Sulfur Compound Extraction and Sweetening | |
Ch. 11.1 | KBR Refinery Sulfur Management | |
Ch. 11.2 | Belco EDV Wet Scrubbing System: Best Available Control Technology (BACT) for FCCU Emission Control | |
Ch. 11.3 | UOP Merox Process | |
Ch. 11.4 | The S Zorb Sulfur Removal Technology Applied to Gasoline | |
Ch. 11.5 | ConocoPhillips S Zorb Diesel Process | |
Ch. 11.6 | Gasoline Desulfurization | |
Pt. 12 | Visbreaking and Coking | |
Ch. 12.1 | ConocoPhillips Delayed Coking Process | |
Ch. 12.2 | FW Delayed-Coking Process | |
Ch. 12.3 | FW/UOP Visbreaking Process | |
Pt. 13 | Oxygenates Production Technologies | |
Ch. 13.1 | Huls Ethers Processes | |
Ch. 13.2 | UOP Ethermax Process for MTBE, ETBE, and TAME Production | |
Ch. 13.3 | UOP Olefin Isomerization | |
Ch. 13.4 | Oxypro Process | |
Pt. 14 | Hydrogen Processing | |
Ch. 14.1 | Hydrogen Processing | |
Pt. 15 | Gas-to-Liquids Technologies | |
Ch. 15.1 | Olefin Production from Methanol | |
Ch. 15.2 | The Syntoleum Process of Converting Natural Gas into Ultraclean Hydrocarbons | |
Ch. 15.3 | Shell Middle Distillate Synthesis (SMDS) Process | |
Glossary | ||
Abbreviations and Acronyms | ||
Index |
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