Figure 3.6 Characterizing Boiling Points of Petroleum Fractions (From API Technical Data Book).Figure 3.5 The True Boiling Point (TBP) distillation apparatus.Temperature (☌) of TBP, ASTM D86, D86 (Crack reduced), ASTM D1160 (Vac), ASTM D1160 (Am) and ASTM D2887 of distillation blend (Courtesy of Honeywell UniSim software, Honeywell (R) and UniSim (R) are registered trademarks of Honeywell International Inc.). Figure 3.4 Snapshot of liquid volume (%) vs.
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Temperature (☌) of TBP and ASTM D86 plots of distillation blend (Courtesy of Honeywell UniSim software, Honeywell (R) and UniSim (R) are registered trademarks of Honeywell International Inc.).
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Figure 2.9 Poly nuclear aromatic hydrocarbons.Figure 2.8 Substitution by a naphthenic ring.Figure 2.7 Substitution by other aromatics.Figure 2.6 Structural formulas of xylene.Figure 2.4 Benzene ring illustrated in Kekule’s formula.Figure 2.2 Branched chain aliphatic compounds.Figure 2.1a Straight chain hydrocarbon compounds.Figure 2.1 Classification of hydrocarbons.Figure 1.5 Petrochemical flow scheme (Source: UOP – A Honeywell Co.).Figure 1.4 Refining flow scheme (source: UOP – A Honeywell Co.).(Source: OPEC Annual Statistical Bulletin, 2012). (Source: Gelder, Alan, Hydrocarbon Processing, pp 25, February 2015 ). Figure 1.2 Regional gross refining margins, US$/bbl.Figure 1.1 Quarterly global demand outlook 2014 – 2015 (Source: Gelder, Alan, pp 25.Appendix D: A List of Engineering Process Flow Diagrams and Process Data Sheets.Appendix C: Physical and Chemical Characteristics of Major Hydrocarbons.B.13 Homogeneous Second Order Linear Differential Equation with Constant Coefficients.B.8 Exponential / Logarithmic Functions.B.3 Liebnitz’s Rule – Higher Derivatives of Products.B.2 General and Trigonometric Functions.Glossary of Petroleum and Technical Terminology.12.14 Cause – Loss of Glycol Out of Still Column.12.11 Kremser-Brown-Sherwood Method-No Heat of Absorption.12.9 Process Description of Gas Processing using UniSim ® Simulation.12.2 Diesel Hydrodesulfurization (DHDS).Chapter 12: Gas Processing and Acid Gas Removal.11.9 Pressure Swing Adsorption (PSA) Unit.11.1 Hydrogen Requirements in a Refinery.Chapter 11: Hydrogen Production and Purification.10.15 Chemical Release and Flash Fire: A Case Study of the Alkylation Unit at the Delaware City Refining Company (DCRC) Involving Equipment Maintenance Incident.10.14 Chevron – Honeywell UOP Ionic liquid Alkylation.10.13 A New Technology of Alkylation Process Using Ionic Liquid.10.11 HF and H 2SO 4 Mitigating Releases.10.9 Kinetics and Thermodynamics of Alkylation.Chapter 10: Alkylation and Polymerization Processes.9.15 Modeling of Naphtha Catalytic Reforming Process.Chapter 9: Catalytic Reforming and Isomerization.8.16 Health, Safety and Environment Considerations.8.15 Troubleshooting for Fluidized Catalyst Cracking Units.8.13 Refining/Petrochemical Integration.8.10 Estimating Potential Yields of FCC Feed.7.23 Health, Safety and Environment Considerations.7.22 Atmospheric Residue Desulfurization.7.14 Factors Affecting Hydrocracking Process Operation.7.9 Process Design, Rating and Performance.7.8 Thermodynamics and Kinetics of Hydrocracking.
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6.17 Health, Safety and Environment Considerations.6.13 Safety and Environmental Considerations.6.4 Simulation of Vacuum Distillation Unit.5.8 Health, Safety and Environment Considerations.
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