Open AccessBook
Petroleum Refining: Technology and Economics
James H. Gary,Glenn Handwerk +1 more
- 01 Jan 1993
886
TL;DR: In this article, Yarsintez et al. presented an economic model for delayed Coking operation and delay Coking process, and showed that delay can increase the costs of Coking and Coking operations.
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Abstract: Introduction Refinery Processes and Operations Historic Overview Product Demand and Supply U.S. Statistics World Statistics Industry Characteristics Refinery Economics Cost Estimation Refinery Complexity Refinery Flow Scheme and Chapter Outline Refinery Products Low-Boiling Products Gasoline Gasoline Specifications Distillate Fuels Residual Fuel Oils Refinery Feedstocks Crude Oil Properties Composition of Petroleum Crudes Suitable for Asphalt Manufacture Crude Distillation Desalting Crude Oils Atmospheric Topping Unit Vacuum Distillation Auxiliary Equipment Crude Distillation Unit Products Case-Study Problem: Crude Units Coking and Thermal Processes Types, Properties, and Uses of Petroleum Coke Process Description-Delayed Coking Operation-Delayed Coking Process Description-Flexicoking Process Description-Fluid Coking Yields from Flexicoking and Fluid Coking Capital Costs and Utilities for Flexicoking and Fluid Coking Visbreaking Case-Study Problem: Delayed Coker Catalytic Cracking Fluidized Bed Catalytic Cracking New Designs for Fluidized Bed Catalytic Cracking Units Cracking Reactions Cracking of Paraffins Olefin Cracking Cracking of Naphthenic Hydrocarbons Aromatic Hydrocarbon Cracking Cracking Catalysts FCC Feed Pretreating Process Variables Heat Recovery Yield Estimation Capital and Operating Costs Case-Study Problem: Catalytic Cracker Catalytic Hydrocracking Hydrocracking Reactions Feed Preparation The Hydrocracking Process Hydrocracking Catalyst Process Variables Hydrocracking Yields Investment and Operating Costs Modes of Hydrocracker Operation Case-Study Problem: Hydrocracker Hydroprocessing and Resid Processing Composition of Vacuum Tower Bottoms Processing Options Hydroprocessing Expanded-Bed Hydrocracking Processes Moving-Bed Hydroprocessors Solvent Extraction Summary of Resid Processing Operations Hydrotreating Hydrotreating Catalysts Aromatics Reduction Reactions Process Variables Construction and Operating Costs Case-Study Problem: Hydrotreaters Catalytic Reforming and Isomerization Reactions Feed Preparation Catalytic Reforming Processes Reforming Catalyst Reactor Design Yields and Costs Isomerization Capital and Operating Costs Isomerization Yields Case-Study Problem: Naphtha Hydrotreater, Catalytic Reformer, and Isomerization Unit Alkylation and Polymerization Alkylation Reactions Process Variables Alkylation Feedstocks Alkylation Products Catalysts Hydrofluoric Acid Processes Sulfuric Acid Alkylation Processes Comparison of Processes Alkylation Yields and Costs Safety Issues Polymerization Case-Study Problem: Alkylation and Polymerization Product Blending Reid Vapor Pressure Octane Blending Blending for Other Properties Case-Study Problem: Gasoline Blending Octane Calculations for Pool Gasoline Case-Study Problem: Diesel and Jet Fuel Blending Supporting Processes Hydrogen Production and Purification Gas Processing Unit Acid Gas Removal Sulfur Recovery Processes Ecological Considerations in Petroleum Refining Wastewater Treatment Control of Atmospheric Pollution Noise Level Control Case-Study Problem: Saturated Gas Recovery, Amine, and Sulfur Recovery Units Refinery Economics and Planning Linear Programming Overview Refinery Linear Programming Models Economics and Planning Applications Lubricating Oil Blending Stocks Lube Oil Processing Propane Deasphalting Viscosity Index Improvement and Solvent Extraction Viscosity Index Improvement and Hydrocracking Dewaxing Hydrofinishing Finishing by Clay Contacting Environmental Impacts Petrochemical Feedstocks Aromatics Production Unsaturate Production Saturated Paraffins Additives Production from Refinery Feedstocks Use of Alcohols and Ethers Ether Production Reactions Ether Production Processes Yields Costs for Ether Production Production of Isobutylene Commercial Dehydrogenation Processes Houdry's CATOFIN ConocoPhillips Petroleum's Star UOP LLC OLEFLEX Snamprogetti Yarsintez Process Costs to Produce Isobutylene from Isobutane International Union of Pure and Applied Chemists Nomenclature Isooctene and Isooctane Production Cost Estimation Rule-of-Thumb Estimates Cost-Curve Estimates Major Equipment Factor Estimates Definitive Estimates Summary Form for Cost Estimates Storage Facilities Land and Storage Requirements Steam Systems Cooling Water Systems Other Utility Systems Application of Cost Estimation Techniques Economic Evaluation Definitions Return on Original Investment Payout Time Discounted Cash Flow Rate of Return Case-Study Problem: Economic Evaluation Case-Study Problem: Economic Solution Appendix A: Definitions of Refining Terms Appendix B: Physical Properties Appendix C: U.S. Bureau of Mines Routine Analyses of Selected Crude Oils Appendix D: Economic Evaluation Example Problem Appendix E: Photographs Index *Most chapters include Problems, Notes, and Additional Reading sections
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Citations
NiMo/MCM-41 Catalysts for the Hydrotreatment of Polychlorinated Biphenyls
Franklin J. Méndez,Ernesto Bastardo-González,Paulino Betancourt,Paulino Betancourt,Luis Paiva,Joaquín L Brito +5 more
TL;DR: In this paper, MCM-41 type mesoporous materials of pure silicon and aluminosilicates (with Si/Al atomic ratios of 20 and 40) were prepared by a facile synthesis method and used to support NiMo catalysts.
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Disaggregation–aggregation based model reduction for refinery-wide optimization
Taoufiq Gueddar,Vivek Dua +1 more
TL;DR: Reduced nonlinear refinery models are developed by generating and using input–output data from a process simulator using rigorous process models of continuous catalytic reformer and naphtha splitter units for generating the data.
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Quantifying carbon capture potential and cost of carbon capture technology application in the U.S. refining industry
TL;DR: In this article, bottom-up modeling and techno-economic analysis approaches are integrated to quantify the national CO2 emission reduction potential and costs of three types of carbon capture technologies applied to U.S. refineries.
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Global sourcing in oil markets
TL;DR: The authors developed a multi-country general equilibrium model that incorporates crude oil global sourcing by refineries and refined oil demand by downstream industries that are connected through international trade and input-output linkages.
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Abatement costs of CO2 emissions in the Brazilian oil refining sector
David Alves Castelo Branco,Alexandre Szklo,Gabriel Lourenço Gomes,Bruno Soares Moreira Cesar Borba,Roberto Schaeffer +4 more
TL;DR: In this paper, the authors estimate the abatement costs of CO2 emissions of the Brazilian oil refining sector and find that the most promising alternative is thermal energy management, whose cost equals US$20/t CO2 at 8% p.a. discount rate.
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