By Hassan E. Alfadala, G.V. Rex Reklaitis and Mahmoud M. El-Halwagi (Eds.)
Content material:
Copyright
, Page iv
Preface
, Pages x-xi, Hassan Alfadala, G.V. Rex Reklaitis, Mahmoud El-Halwagi
International Technical Committee
, Pages xii-xiii
A Multi-Paradigm power version for Liquid average fuel Analysis
, Pages 1-9, Bri-Mathias S. Hodge, Joseph F. Pekny, Gintaras V. Reklaitis
Dynamic Optimization of the LNG worth Chain
, Pages 10-18, Bjarne A. Foss, Ivar J. Halvorsen
Liquefaction expertise; advancements via History
, Pages 19-31, Paul Bosma, Rob Klein Nagelvoort
The Globalization of LNG Markets: ancient Context, present traits and clients for the Future
, Pages 32-43, Susan L. Sakmar, Donald R. Kendall Jr.
The Liquefied strength Chain
, Pages 44-52, Audun Aspelund, Truls Gundersen
A common method in accordance with SIMAR for Composing and comparing Expander - dependent Processes
, Pages 53-60, Carlos Yengle, Stanley Huang
Application of Hybrid Coolers for Base Load LNG Liquefaction Plants
, Pages 61-69, J.C. Kuo, Peter G. Demakos
Cost Estimation and Optimization of the Topping Unit items on the regular nation Condition
, Pages 70-78, Nasser Saghatoleslami, Fanaei Shikholeslami, Farhad Shahraki, Younas Dadmohamadi
Minimum strength Operation of Petlyuk Distillation Columns - Nonsharp Product Specifications
, Pages 79-87, Ivar J. Halvorsen, Sigurd Skogestad
The Engineering of Compact Exchangers to Required Dimensions
, Pages 88-95, M. Picón Núñez, C.E. Carreón, G.T. Polley
Towards the dynamic initialization of C4 splitter models
, Pages 96-103, Ivan Dones, Heinz A. Preisig, Stefan de Graaf
An assessment of recent Methodologies for the layout of Cryogenic strategies with an emphasis on LNG
, Pages 104-112, Truls Gundersen, Audun Aspelund, Paul I. Barton
A Shortcut Thermodynamic version for Simulating LNG Liquefaction Facilities
, Pages 113-121, Stanley Huang, Nancy Tsai, Pankaj Shah
Phase habit matters for Multicomponent ordinary Gas-Like Mixtures
, Pages 122-130, M. Atilhan, J. Zhou, S. Ejaz, D. Cristancho, J. Holste, K.R. Hall
Simulation and effort Integration of a Liquefied usual gasoline (LNG) Plant
, Pages 131-135, Saad A. Al-Sobhi, Hassan E. Alfadala, Mahmoud M. El-Halwagi
Wide variety, excessive Accuracy PρT Measurements through unmarried Sinker Magnetic Suspension Densimeter for normal Gas-Like Mixtures
, Pages 136-142, M. Atilhan, P.V. Patil, S. Ejaz, D. Cristancho, J. Holste, K.R. Hall
A temporary Operational making plans version for a LNG construction System
, Pages 143-153, Ajay Selot, Loi Kwong-Kuok, Mark Robinson, Thomas L. Mason, Paul I. Barton
Development in combined Refrigerant Cycles utilized in Olefin Plants
, Pages 154-161, M. Mafi, M. Amidpour, S.M. Mousavi Naeynian
Nuclear expertise for Frontier Advances within the average gasoline Industry
, Pages 162-170, Rusi P. Taleyarkhan
A strategy for optimum Operation of bathroom Compressors in a LNG Gasification Plant
, Pages 171-178, Myung Wook Shin, Namjin Jang, Dongil Shin, Chonghun Han, Soo Hyoung Choi, En Sup Yoon
Optimizing Compressor Operations in an LNG Plant
, Pages 179-184, M.M. Faruque Hasan, Iftekhar A. Karimi, Hassan E. Alfadala
Synthesis of warmth Exchanger Networks regarding part Changes
, Pages 185-192, M.M. Faruque Hasan, Iftekhar A. Karimi, Hassan E. Alfadala
Towards a Framework for Systematic Innovation of Catalytic fuel Conversion Processes
, Pages 193-201, Patrick Linke, David Linke, Daniel Montolio-Rodriguez
Maintenance matters in oil and fuel procedures: Detection of valve stiction
, Pages 202-210, Salim Ahmed, Sirish L. Shah, Biao Huang
Single-cycle mixed-fluid LNG technique half I: optimum design
, Pages 211-218, Jørgen Bauck Jensen, Sigurd Skogestad
Single-cycle mixed-fluid LNG approach half II: optimum operation
, Pages 219-226, Jørgen Bauck Jensen, Sigurd Skogestad
Unlocking the possibility of smooth regulate and Optimization innovations in LNG Production
, Pages 227-238, Wilco Sturm, Maria Parra-Calvache, Francois Chantant, Jan van Opstal
CO2 seize by means of Novel Amine Blends
, Pages 239-246, Prakash D. Vaidya, Eugeny Y. Kenig
PVA/PVAm combination FSC Membrane for common fuel Sweetening
, Pages 247-255, Liyuan Deng, Taek-Joong Kim, Marius Sandru, May-Britt Hägg
Simulation of an Acid fuel elimination strategy utilizing Methyldiethanolamine; an Equilibrium Approach
, Pages 256-265, Hassan E. Alfadala, Essa Al-Musleh
Simulation of the method of organic removing of Hydrogen Sulfide from Gas
, Pages 266-275, E.M. Elkanzi
Solubility of Sulfur in bitter fuel Mixtures
, Pages 276-285, John J. Carroll
Asset administration Practices at Qatargas
, Pages 286-296, Abdel Kader Attou, Qadeer Ahmed
Risk dependent Integrity Modeling of fuel Processing amenities utilizing Bayesian Analysis
, Pages 297-306, Premkumar Thodi, Faisal Khan, Mahmoud Haddara
Safety of Buried Pressurized fuel Pipelines close to Explosion Sources
, Pages 307-316, Fotis Rigas
Shipboard Reliquefaction for giant LNG Carriers
, Pages 317-324, Thomas N. Anderson, Mark E. Ehrhardt, Robert E. Foglesong, Tom Bolton, David Jones, Andy Richardson
Safety review of LNG Terminal curious about the end result research of LNG Spills
, Pages 325-331, Jamin Koo, Ho Soo Kim, received So, Ku Hwoi Kim, En Sup Yoon
Towards a Holistic method of the Sustainable Use of Seawater for strategy Cooling
, Pages 332-340, Ahmed Abdel-Wahab, Patrick Linke, Hassan Alfadala, Mahmoud El-Halwagi, invoice Batchelor
Transport and destiny of Chlorinated By-Products linked to Cooling Water Discharges
, Pages 341-353, Adeyinka E. Adenekan, Venkat S. Kolluru, Joseph P. Smith
Comparative financial research of Gas-to-Liquid strategies for optimum Product Selection
, Pages 354-361, Chul-Jin Lee, Chonghun Han
GTL Feed via Catalytic Oxidation of Methane in Plate Reactor
, Pages 362-369, Mohamed A. Nakoua, Muftah H. El-Naas
Scale-up and Demonstration of Fischer-Tropsch Technology
, Pages 370-377, Dag Schanke, Matthias Wagner, Patrick Taylor
Shell GTL, from Bench scale to global scale
, Pages 378-386, Rob Overtoom, Niels Fabricius, Wim Leenhouts
Model-based retrofit layout and research of petrochemical processes
, Pages 387-393, Jamal Rashed, Rafiqul Gani
Natural gasoline Conversion to Ethylene: An Experimental and Numerical Study
, Pages 394-401, Nakisa Yaghobi, Mir Hamid Reza Ghoreishy
Value production via Integration of Downstream approach Technologies
, Pages 402-414, Mary Jane Hagenson, Bruce Kreischer, William Valerioti, Charles Nease
The VCM strategy Economics: international and uncooked fabric Impacts
, Pages 415-422, Farid Benyahia
An method of the layout of complicated Fischer-Tropsch Reactor for Operation in Near-Critical and Supercritical part Media
, Pages 423-433, Nimir O. Elbashir, Buping Bao, Mahmoud M. El-Halwagi
Index
, Pages 434-441
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Additional resources for Proceedings of the 1st Annual Gas Processing Symposium. 10–12 January 2009, Doha, Qatar
Sample text
The LCO2 together with LIN is transported offshore in the combined gas carrier, providing enhanced utilization of the ship. This paper is an executive summary of four papers by A. Aspelund and T. Gundersen, (2007 a, b, c ,d), describing the concept and the processes in greater detail. An extensive list of references may be found in these papers. 2. The offshore LNG process Figure 2 shows a configuration of the offshore natural gas liquefaction process. After heat exchange, the CO2 is still in liquid form at ambient temperature and is pumped to injection pressure and injected for EOR.
Qatar’s expansion of LNG handling capacity will enable Qatar to continue to capitalize on the benefits of its resources and to further diversify its client base. Qatar is already the largest single supplier to the Asian market and additional handling capacity will enable Qatar to increase exports to other growing markets around the world. An additional benefit to the Qatari LNG industry is the fact that Qatar is equidistant in shipping terms between the Atlantic and Asia/Pacific markets. This geographical benefit will enable Qatar to become the world’s largest LNG “swing producer” in the near future.
The gas engine electric propulsion plant and fuel tanks is placed in the aft. The ship characteristics are presented in Table 1 and a principal sketch of the general arrangements is shown in Figure 3. Table 1 Ship main characteristics Length between perpendiculars Breadth Depth Draft Cargo capacity Service speed Installed power Propulsion Number of tanks Ship Utilization Factor Loading/offloading system 150 [m] 24 [m] 14,2 [m] 9,5 [m] 13000 [m3] 16 [knots] 6000 [kW] Gas-fuelled power generation 10 60 % Submerged turret loading The Liquefied Energy Chain 47 Figure 3 Ship design and tank arrangement In order to make the LNG production run continuously, one ship will at all times be tied up in offshore operations.