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Sour Gas and Related Technologies by Ying Wu, John J. Carroll, Weiyao Zhu

Posted On February 25, 2017 at 3:20 pm by / Comments Off on Sour Gas and Related Technologies by Ying Wu, John J. Carroll, Weiyao Zhu

By Ying Wu, John J. Carroll, Weiyao Zhu

Carbon dioxide has been implicated within the international weather swap, and CO2 sequestration is a expertise being explored to lower the anthropogenic emission of CO2 into the ambience. The injection of CO2 for more suitable oil restoration (EOR) has the duel good thing about sequestering the CO2 and increasing the lifetime of a few older fields. This quantity provides a number of the most recent details on those approaches masking actual houses, operations, layout, reservoir engineering, and geochemistry for AGI and the comparable technologies.Content:
Chapter 1 Equilibrium Water content material Measurements for Acid gasoline at excessive Pressures and Temperatures (pages 1–20): Francis Bernard, Robert A. Marriott and Binod R. Giri
Chapter 2 Comparative research on fuel Deviation issue Calculating versions for CO2 wealthy fuel Reservoirs (pages 21–36): Nan Zhang, Xiao Guo, Qiang Zhang, Rentian Yan and Yan Ran
Chapter three H2S Viscosities and Densities at High?Temperatures and Pressures (pages 37–47): Binod R. Giri, Robert A. Marriott and Pierre Blais
Chapter four Solubility of Methane in Propylene Carbonate (pages 49–55): Fang?Yuan Jou, Kurt A.G. Schmidt and Alan E. Mather
Chapter five A Holistic examine gasoline Treating Simulation (pages 57–78): Nathan A. Hatcher, R. Scott Alvis and Ralph H. Weiland
Chapter 6 managed Freeze sector™ advertisement Demonstration Plant Advances know-how for the Commercialization of North American bitter fuel assets (pages 79–90): R.H. Oelfke, R.D. Denton and J.A. Valencia
Chapter 7 Acid fuel Dehydration – A DexPro™ expertise replace (pages 91–115): Jim Maddocks, Wayne McKay and Vaughn Hansen
Chapter eight a glance at good CO2 Formation in numerous excessive CO2Concentration Depressuring eventualities (pages 117–128): James van der Lee, John J. Carroll and Marco Satyro
Chapter nine capability websites and Early possibilities of Acid gasoline Re?injection in China (pages 129–142): Qi Li, Xiaochun Li, Lei Du, Guizhen Liu, Xuehao Liu and Ning Wei
Chapter 10 Acid gasoline Injection for a Waste movement with Heavy Hydrocarbons and Mercaptans (pages 143–152): Xingyuan Zhao, John J. Carroll and Ying Wu
Chapter eleven Compression of Acid gasoline and CO2 with Reciprocating Compressors and Diaphragm Pumps for garage and stronger Oil restoration (pages 153–164): Anke Braun, Josef Jarosch, Rainer Dubi and Luzi Valar
Chapter 12 research of using Choke Valves in Acid gasoline Compression (pages 165–181): James van der Lee and Edward Wichert
Chapter thirteen The Kinetics of H2S Oxidation by means of hint O2 and Prediction of Sulfur Deposition in Acid gasoline Compression platforms (pages 183–214): N. I. Dowling, R. A. Marriott, A. Primak and S. Manley
Chapter 14 Blowout Calculations for Acid fuel good with excessive Water reduce (pages 215–226): Shouxi Wang and John J. Carroll
Chapter 15 effect of Sulfur Deposition on fuel Reservoir improvement (pages 227–245): Weiyao Zhu, Xiaohe Huang, Yunqian lengthy and Jia Deng
Chapter sixteen Modeling and evaluate of Oilfield Fluid Processing Schemes (pages 247–260): Jie Zhang, Ayodeji A. Jeje, Gang Chen, Haiying Cheng, Yuan You and Shugang Li
Chapter 17 Optimization of the choice of Oil?Soluble Surfactant for reinforcing CO2 Displacement potency (pages 261–272): Ping Guo, Songjie Jiao, Fu Chen and Jie He

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03 K. The viscometer temperature was measured with a built-in resistant temperature detector (RTD) mounted to the base of the Inconel-718 measurement chamber. 3·3 Results and Discussion As stated earlier, the performance of the instruments including the accuracy and reproducibility of the measurements previously have been assessed and discussed in detail [2]. 2 kg m 3 for the entire range of temperatures and pressures covered in this study ( T = 273 to 423 K and p < 100 MPa). 2) shows the density isotherms measured at T = 273, 323, 373 and 423 K and at pressures up to p = 100 MPa.

K. Barua, /. Phys. , 3,526-535 (1970). 15. K. Bhattacharya, /. Chem. Phys. 53, 893-895 (1970). 16. D. Steele, D. H. Chem. 55,129-199 (1906). 17. G. Jung and H. Chem. 7,130-147 (1930). 18. H. Preston-Thomas, 'The International Temperature Scale of 1990 (ITS-90)," Metrologia 27, 3-10 (1990). G. Schmidt,1 and Alan E. Mather* Department of Chemical and Materials Engineering University of Alberta, Edmonton, AB Canada Present address: Schlumberger-DBR Technology Center, Edmonton, Alberta *To whom correspondence should be addressed.

Rend. Acad. Sei. URSS. 30, 625-628 (1941). 30. V. Kiss, I. Lajtai, and G. Thury, Z. Anorg. Allg. Chem. 223, 346-352 (1937). 31. F. Pollitzer, Z. Anorg. Chem. 64,121-148 (1909). 32. H. Gamsjäger, W. Rainer, and P. Schindler, Monatsh. Chem. 98,1793-1802 (1967). 33. J. Kendall and J. C. Andrews, /. Am. Chem. Soc. 43,1545-1560, (1921) 34. W. Gerrard, J. Appl. Chem. Biotechnol. 22,623-650 (1972). 35. A. P. Riley, Deep-Sea Res. 26A, 259-268 (1979). 2 Comparative Study on Gas Deviation Factor Calculating Models for C0 2 Rich Gas Reservoirs Nan Zhang, Xiao Guo, Qiang Zhang, Rentian Yan, and Yan Ran State Key Laboratory of Oil and Gas Reservoir Geology and Exploitation Southwest Petroleum University Chengdu 610500 China Abstract The application of traditional classical equations of state to calculate the physical property parameters of a sour gas mixture can result in significant errors.

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