III
Energy
9 Fossil Fuel Emilio Diaz-Bejarano, Sandro Macchietto, Andrey V. Porsin, Davide Manca, and Valentina Depetri
Energy Efficient Thermal Retrofit Options for Crude Oil Transport in Pipelines • Process Industry Economics of Crude Oil and Petroleum Derivatives for Scheduling, Planning, and Feasibility Studies
10 Bio Fuel Sumaiya Zainal Abidin, Basudeb Saha, Raj Patel, Amir Khan, I. M. Mujtaba, Richard Butterfield, Elisabetta Mercuri, and Davide Manca
Environmentally Benign Biodiesel Production from Renewable Sources • Process for Synthesis of Biodiesel from Used Cooking Oil: Feasibility and Experimental Studies
11 Synthetic Fuel and Renewable Energy N. O. Elbashir, Wajdi Ahmed, Hanif A. Choudhury, Nasr Mohammad Nasr, Naila Mahdi, Kumaran Kannaiyan, Reza Sadr, Rajasekhar Batchu, Kalpesh Joshi, Naran M. Pindoriya, Haile-Selassie Rajamani, N. O. Elbashir, Laial Bani Nassr, and Mohamed Ghouri
Gas-to-liquid (GTL)-Derived Synthetic Fuels: Role of Additives in GTL-Derived Diesel Fuels • The Role of Alternative Aviation Fuels on Reducing the Carbon Footprint • Integration of Distributed Renewable Energy Generation with Customer-End Energy Management System for Effective Smart Distribution Grid Operation • Evaluation and Modeling of Demand and Generation at Distribution Level for Smart Grid Implementation • A Process to Model Fischer–Tropsch Reactors
12 Carbon Capture Atuman S. Joel, Eni Oko, Meihong Wang, Colin Ramshaw, Xiaobo Luo, Eni Oko, Akeem K. Olaleye, Jonathan G. M. Lee, KeJun Wu, DoYeon Kim, Nilay Shah, C. Kolster, N. Mac Dowell, Lin Ma, Mohamed Pourkashanian, S. Brown, Adekola Lawal, H. Mahgerefteh, R. T. J. Porter, S. Martynov, M. Fairweather, R. M. Woolley, S. A. E. G. Falle, G. C. Boulougouris, Ioannis G. Economou, D. M. Tsangaris, I. K. Nikolaidis, A. Beigzadeh, C. Salvador, K. E. Zanganeh, A. Ceroni, R. Farret, Y. Flauw, J. Hébard, D. Jamois, C. Proust, S. Y. Chen, J. L. Yu, Y. Zhang, D. Van Hoecke, R. Hojjati Talemi, S. Cooreman, J. Bensabat, R. Segev, D. Rebscher, J. L. Wolf, A. Niemi, Mert Atilhan, Ruh Ullah, Cafer T. Yavuz, Nejat Rahmanian, and Sina Gilassi
Application of Rotating Packed Bed Technology for Intensified Postcombustion CO2 Capture Based on Chemical Absorption • Process Simulation and Integration of Natural Gas Combined Cycle (NGCC) Power Plant Integrated with Chemical Absorption Carbon Capture and Compression • Postcombustion CO2 Capture Based on Chemical Absorption in Power Plants Operation of Supercritical Coal-Fired Power Plant (SCPP) Integrated with CO2 Capture under the UK Grid Code • Whole System Experimental and Theoretical Modeling Investigation of the Optimal CO2 Stream Composition in the Carbon Capture and Sequestration Chain • Performance of Porous Covalent Organic Polymers for CO2 Capture at Elevated Pressure • Postcombustion Carbon Capture Using Polymeric Membrane
9
Fossil Fuel
Emilio Diaz-Bejarano and Sandro Macchietto
Imperial College London
Andrey V. Porsin
Boreskov Institute of Catalysis and UNICAT Ltd
Davide Manca, Valentina Depetri
Politecnico di Milano - Italy
9.1 Energy Efficient Thermal Retrofit Options for Crude Oil Transport in Pipelines Emilio Diaz-Bejarano, Andrey V. Porsin, and Sandro Macchietto
Introduction • Drag Reduction and Prevention of Wax Deposition • Thermo-Hydraulic Model of Pipelines with Intermediate Point Heating • Case Studies • Conclusions
Acknowledgment
Subscripts
References
9.2 Process Industry Economics of Crude Oil and Petroleum Derivatives for Scheduling, Planning, and Feasibility Studies Davide Manca and Valentina Depetri
Introduction • Introduction to CO • CO Production, Consumption, Reserves, and Refinery Capacities • The Fundamentals of CO and Derivatives Markets • The Fundamentals of CO and Derivatives Markets
CO Price Forecast • Economics of Derivatives • Applications Discussion • Conclusions
List of Abbreviations
References
9.1 Energy Efficient Thermal Retrofit Options for Crude Oil Transport in Pipelines
Diaz-Bejarano Emilio, Porsin Andrey V., Macchietto Sandro
9.1.1 Introduction
Pipelines are used to transport large amounts of crude oil over large distances (either overland or subsea), representing the most economical alternative. Flow assurance faces two main problems: viscosity increase due to gradual cooling of the oil along the pipeline and fouling deposition. These problems are especially important in very cold environments (Russia, Alaska, North Sea, deep oceanic waters, etc.) and when dealing with nonconventional oils, usually heavy or extra-heavy oil and waxy oils. In many cases, the depletion of deposits in conventional oil reservoirs is gradually leading to more extraction of these types of feedstock from remote locations. All these situations result in pipeline transport difficulties such as increased pumping costs, reduced flow rates, and the possibility of flow inhibition or blockage, with potentially major economic impact (Correra et al., 2007; Martínez-Palou et al., 2011).
Crude oils are usually classified according to their American Petroleum Institute (API) gravity, which relates specific gravity of oil at 60 F to that of water at 60 F, as shown in this chapter, Table 9.1 (Riazi, 2005). Normally, the heavier the oil, the more viscous it is. Petroleum viscosity (μ) increases exponentially as temperature decreases. Pressure drop along a pipe of given diameter increases with viscosity. Hence, if crude oil is cooled down to low temperatures it becomes very difficult to transport. The problem is even more significant when transporting heavy and extra-heavy oil, which present high viscosity (103–106 cP) even at mild temperature conditions, normally due to high asphaltenes content (Martínez-Palou et al., 2011). A pipeline designed for low viscosity oils may not be able to handle the transition to heavier oils without some adaptation.
TABLE 9.1 Categorization of Crude Oils according to API Gravity
| Light | Conventional | Heavy | Extra-Heavy |
API | >35 | 35–20 | 20–10 | <10 |
μ (cP) at room T | <10 | 10–100 | 100–10,000 | Up to 106 |
Oils with high content of heavy paraffinic hydrocarbons (waxy oils) are also problematic (Aiyejina et al., 2011). At temperatures below the cloud point (or wax appearance temperature, WAT), waxes start solidifying, leading to a significant increase in viscosity. When cooling is restricted to the wall of the pipe, these solids precipitate forming a fouling layer. If cooling affects the bulk of the fluid, it may lead to flow blockage due to gelling (Arnold and Gebhart, 2000). The modeling of wax deposition has drawn the attention of many researches over the past years and many mathematical models have been presented (Kok and Saracoglu, 2000; Singh et al., 2001; Correra et al., 2007; Edmonds et al., 2008; Eskin et al., 2014). In the case of offshore subsea pipelines, the high pressure required by the deep location, combined with the cold temperature of deep waters, may lead to additional deposition problems due to the formation of hydrates that can cause pipe blockage (Mehta et al., 2006).
Current and under development techniques for drag reduction and wax prevention in pipelines are reviewed in the following section. In this work, a thermal strategy using single- and mul...