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E-raamat: Crude Oil Refining: A Simplified Approach [Taylor & Francis e-raamat]

  • Formaat: 267 pages, 10 Tables, black and white; 24 Line drawings, black and white; 117 Halftones, black and white; 141 Illustrations, black and white
  • Ilmumisaeg: 04-Oct-2022
  • Kirjastus: CRC Press
  • ISBN-13: 9781003291824
  • Taylor & Francis e-raamat
  • Hind: 147,72 €*
  • * hind, mis tagab piiramatu üheaegsete kasutajate arvuga ligipääsu piiramatuks ajaks
  • Tavahind: 211,02 €
  • Säästad 30%
  • Formaat: 267 pages, 10 Tables, black and white; 24 Line drawings, black and white; 117 Halftones, black and white; 141 Illustrations, black and white
  • Ilmumisaeg: 04-Oct-2022
  • Kirjastus: CRC Press
  • ISBN-13: 9781003291824
This book provides an overview of crude oil refining processes and presents a deep analysis of the current context and challenges imposed on players in the downstream industry. Crude Oil Refining: A Simplified Approach covers traditional processes of the refining industry, the impact of current trends, and technological routes available to help these players survive in a highly competitive environment.

FEATURES











Offers a simplified approach to crude oil refining processes





Discusses economic information related to the downstream business, including refining margins and profitability





Introduces newer trends in the industry, such as petrochemical integration, crude-to-chemicals refineries, and renewables coprocessing in crude oil refineries





Presents the challenges related to these new trends and offers technological solutions to overcome them for profitable and sustainable operations





Describes how the use of biofuels can minimize the environmental impact of transportation fuel in nations of high demand like Brazil

Offering a contemporary view of current challenges and opportunities in the downstream oil and gas business, this practical book is aimed at readers working in the fields of petroleum and chemical engineering.
Preface ix
Acknowledgments xi
Author xiii
Chapter 1 Crude Oil
1(14)
1.1 Introduction
1(3)
1.2 Primary Treating Processes of Crude Oil
4(3)
1.3 Crude Oil Derivatives
7(8)
Chapter 2 Crude Oil Distillation
15(8)
2.1 Crude Oil Distillation Units
15(4)
2.2 Vacuum Distillation Section
19(4)
Chapter 3 Thermal Conversion Processes
23(12)
3.1 Visbreaking Process
23(2)
3.2 Delayed Coking Process
25(5)
3.3 Solvent Deasphalting Technologies
30(5)
Chapter 4 Catalytic Conversion Processes
35(38)
4.1 Fluid Catalytic Cracking (FCC) Units
35(4)
4.2 Residue Fluid Catalytic Cracking (RFCC) Technologies
39(3)
4.3 The FCC Catalyst: Converting Residues to Added-Value Derivatives
42(1)
4.4 Meeting the Market Demand through FCC Optimization
43(2)
4.5 The Petrochemical FCC Alternative: Raising Competitive Advantage
45(4)
4.5.1 Propylene Production from FCC
46(3)
4.6 Catalytic Reforming Technologies
49(7)
4.6.1 Aromatics Separation Section: Ensuring Maximum Added Value
52(2)
4.6.2 Improving the Yield of Light Aromatics: Molecular Management
54(2)
4.7 Naphtha Alkylation Technologies
56(4)
4.8 Naphtha Isomerization
60(4)
4.9 Light Olefin Condensation
64(2)
4.10 Etherification Technologies
66(3)
4.11 Light Paraffin Dehydrogenation
69(4)
Chapter 5 Hydro-processing Technologies
73(32)
5.1 Naphtha Hydrotreating Technologies
77(5)
5.1.1 Coker Naphtha Hydrotreating
77(2)
5.1.2 FCC Naphtha Hydrotreating Technologies
79(2)
5.1.2.1 A Special Challenge: Diene (Diolefin) Control
81(1)
5.2 Diesel Hydrotreating Units
82(2)
5.3 Bottom Barrel Hydrotreating Technologies (Residue Upgrading)
84(4)
5.4 Atmospheric Residue Desulfurization: A Special Case
88(3)
5.5 Hydrocracking Technologies
91(8)
5.6 The Hydroprocessing Catalysts
99(1)
5.7 Deactivation of Hydroprocessing Catalysts
100(5)
Chapter 6 Lubricating Production Refineries
105(14)
6.1 Closing the Sustainability Cycle: Used Lubricating Oil Recycling
110(4)
6.1.1 Used Lubricating Recycling Technologies
111(3)
6.2 A Glance over the Brazilian Lubricating Market
114(5)
Chapter 7 Refining Configurations
119(18)
7.1 Nelson Complexity Index
125(1)
7.2 The Effect of Crude Oil Slate over the Refining Scheme
126(11)
7.2.1 Heavier Crude Oil Processing
126(7)
7.2.2 Light Crude Oil Processing
133(4)
Chapter 8 Hydrogen Production
137(10)
8.1 Hydrogen and Syngas Production Routes
137(4)
8.2 Renewable Hydrogen Generation Routes: Fundamental Enabler to the Energy Transition
141(1)
8.3 Hydrogen Network and Management Actions
142(5)
8.3.1 The Role of Catalytic Reforming Units in the Refineries' Hydrogen Balance
143(4)
Chapter 9 Caustic Treating Processes
147(8)
9.1 Caustic Treating Technologies
147(5)
9.2 Bender Treating Technologies
152(3)
Chapter 10 Environmental Processes
155(18)
10.1 Sour Water Stripping Technologies
155(3)
10.2 Amine Treating Technologies
158(2)
10.3 Sulfur Recovery Technologies
160(5)
10.4 Water and Wastewater Treatment Technologies
165(8)
10.4.1 Oily Sewer
167(1)
10.4.2 Stormwater Sewer
167(2)
10.4.3 Domestic Sewage
169(1)
10.4.4 Steps of Effluent Treatment
169(1)
10.4.5 API Oil-Water Separator
169(1)
10.4.6 Dissolved Air Flotation
169(1)
10.4.7 Biological Treatment
170(1)
10.4.8 Membrane Bioreactors (MBR)
170(3)
Chapter 11 A New Downstream Industry
173(30)
11.1 What Is Petrochemical Integration?
175(2)
11.2 More Added Value to the Processed Crude: Integrated Refining Schemes
177(1)
11.3 Crude Oil to Chemicals: Zero Fuel and Maximum Added Value
178(16)
11.3.1 Available Crude-to-Chemicals Routes
189(1)
11.3.2 The Residue Upgrading Technologies in the Integration of Refining and Petrochemical Assets
190(2)
11.3.3 Closing the Sustainability Cycle: Plastic Recycling Technologies
192(2)
11.4 Renewables Coprocessing in Crude Oil Refineries
194(9)
11.4.1 Biofuel Production in Brazil
195(1)
11.4.2 Challenges of Renewables Coprocessing in Crude Oil Refineries
196(3)
11.4.3 The Hydrotreated Vegetable Oil (HVO): An Attractive Route to Reach "Green Diesel"
199(4)
Chapter 12 The Propylene Production Gap
203(16)
12.1 Propylene: A Fundamental Petrochemical Intermediate
204(1)
12.2 Propylene Production Routes
205(14)
12.2.1 The Maximum Olefin Operation Mode
207(2)
12.2.2 The Petrochemical FCC Alternative
209(2)
12.2.3 Steam Cracking Units
211(1)
12.2.4 Propane Dehydrogenation
211(3)
12.2.5 Olefin Metathesis
214(1)
12.2.6 Methanol-to-Olefin Technologies (MTO)
214(5)
Chapter 13 Gas-to-Liquid Processing Routes
219(10)
13.1 Gas-to-Liquid Technologies
219(5)
13.1.1 Available Technologies
221(3)
13.2 Ammonia Production Process: An Overview
224(5)
13.2.1 Ammonia Production Technologies: Some Commercial Processes
225(4)
Chapter 14 Business Strategy Models Applied to the Downstream Industry
229(12)
14.1 Porter's Competitive Forces in the Downstream Industry
230(6)
14.2 Changing the Focus: More Petrochemicals and Less Fuel
236(5)
14.2.1 Petrochemical and Refining Integration as a Differentiation Strategy
237(4)
Chapter 15 Corrosion Management in Refining Assets
241(16)
15.1 Naphthenic Corrosion: General Overview
241(2)
15.2 Corrosion in Sour Water Stripping Units
243(3)
15.3 Corrosion Process in Amine Treating Units
246(2)
15.4 Corrosion Processes in FCC Units
248(3)
15.4.1 The Petrochemical FCC: Raising Competitive Advantage x Corrosion Attention
250(1)
15.5 Corrosion Management in Hydroprocessing Units
251(6)
Chapter 16 Energy Management and the Sustainability of the Downstream Industry
257(8)
16.1 Introduction and Context
257(1)
16.2 Simple and Available Alternatives to Energy Optimization
258(4)
16.3 The Impact of the Energy Management on the Greenhouse Gas Emissions
262(3)
Index 265
Marcio Wagner da Silva is a Process Engineer and has experience in the Downstream Industry, in technical and managing positions. He received a PhD in Chemical Engineering from State University of Campinas (UNICAMP), an MBA in Project Management from Federal University of Rio de Janeiro (UFRJ), and an MBA in Digital Transformation at Catholic University of Rio Grande do Sul (PUC-RS).