Zobrazeno 1 - 10
of 135
pro vyhledávání: '"William Y. Svrcek"'
Publikováno v:
Oil and Gas Facilities. 2:52-59
Summary This paper provides details of comprehensive computational-fluid dynamics (CFD)-based studies performed to overcome the separation inefficiencies experienced in a large-scale three-phase separator. It will be shown that the classic design met
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::7b36a569bc5abc817f4671f24e582d71
https://doi.org/10.2118/161036-pa
https://doi.org/10.2118/161036-pa
Publikováno v:
Oil and Gas Facilities. 1:57-68
Summary A realistic computational fluid dynamics (CFD) simulation of a field three-phase separator has been developed. This realistic CFD simulation provides an understanding of both the microscopic and macroscopic features of the three-phase separat
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::3b6a142f6971cefd705f622a87441ba7
https://doi.org/10.2118/161212-pa
https://doi.org/10.2118/161212-pa
Publikováno v:
Chemical Engineering & Technology. 35:323-333
Oilfield separator data ranging from light-oil conditions to heavy-oil conditions were incorporated into suitable two-phase and three-phase computational fluid dynamics (CFD) models to provide improved design criteria for separator design methods. Th
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::a803b3ab3830322f590065d8d33ec74c
https://doi.org/10.1002/ceat.201100351
https://doi.org/10.1002/ceat.201100351
Publikováno v:
The Canadian Journal of Chemical Engineering. 90:1547-1561
The multiphase separators are generally the first and largest process equipment in an oil production platform. This primary separation step is a key element in the oil and gas production facilities in that downstream equipment, such as compressors, a
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::a61791e4194aabd2cbc0cfa3c3715cd0
https://doi.org/10.1002/cjce.20665
https://doi.org/10.1002/cjce.20665
Publikováno v:
The Canadian Journal of Chemical Engineering. 90:956-972
Synthesis of the optimum distillation column sequence (DCS), which incorporates a huge search space composed of both conventional and complex arrangements, is a highly complicated combinatorial problem in the field of chemical process design and opti
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::f81ae54656c17dc3375710caa62144fd
https://doi.org/10.1002/cjce.20589
https://doi.org/10.1002/cjce.20589
Publikováno v:
Chemical Engineering & Technology. 34:296-306
Two computational fluid dynamics (CFD) modeling approaches, the discrete phase model (DPM) and the combination of volume of fluid (VOF) and DPM, are developed to simulate the phase separation phenomenon in four pilot-plant-scale separators. The incip
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::6cd6fe672dd3f8920508facd53fa4504
https://doi.org/10.1002/ceat.201000302
https://doi.org/10.1002/ceat.201000302
Autor:
Asok Kumar Tharanivasan, Parviz Rahimi, Shawn David Taylor, Harvey W. Yarranton, William Y. Svrcek, Daniel Merino-Garcia
Publikováno v:
Energy & Fuels. 23:3971-3980
A previously developed regular solution model was adapted to predict the onset and amount of asphaltene precipitation from crude oil blends diluted with pure n-alkanes or a mixture of toluene and n-heptane. Tests were conducted on nine different crud
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::0cec444a4351b9dd3bf3dfec51c1f846
https://doi.org/10.1021/ef900150p
https://doi.org/10.1021/ef900150p
Publikováno v:
The Canadian Journal of Chemical Engineering. 87:477-492
Synthesis of the optimum conventional (with non-sharp separations) distillation column sequence (DCS) is a challenging problem, in the field of chemical process design and optimization, due to its huge search space and combinatorial nature. In this p
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::edf28bf7950b59f35ad82a4cfc96bd06
https://doi.org/10.1002/cjce.20175
https://doi.org/10.1002/cjce.20175
Publikováno v:
Journal of Canadian Petroleum Technology. 48:54-61
Abstract The saturation pressure and solubility of propane in Athabasca bitumen, as well as the liquid phase densities and viscosities, were measured for temperatures from 10 to 50 °C. Equilibration proved challenging for this fluid mixture and requ
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::f0d073540afe812bac2dc32e30ad4e96
https://doi.org/10.2118/09-01-54
https://doi.org/10.2118/09-01-54
Publikováno v:
Energy & Fuels. 23:366-373
An enhanced form of the temperature-dependent attractive pressure term of the Peng-Robinson equation of state (PR EOS) was developed. The function was developed using experimental vapor pressures from the NIST Standard Reference Data Base #103 as wel
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::034e1cfaa07d4eb29fde719d52d382ab
https://doi.org/10.1021/ef8006855
https://doi.org/10.1021/ef8006855