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Metal-reducing microorganisms in petroleum reservoirsYacob, Shahrakbah, n/a January 2000 (has links)
Metal-reducing microorganisms reduce a variety of metals in metabolic processes
coupled to the oxidation of organic compounds. These bacteria play an important role
in the biogeochemical cycling of metals and organic matter in anaerobic aquatic and
sediment ecosystems. It has been proposed recently that metal-reducing
microorganisms also are active in deep subsurface environments such as petroleum
reservoirs. Only two metal-reducing bacteria have been isolated from petroleum
reservoir fluids, Shewanella putrefaciens and Deferribacter thermophilus. This project
studied the occurrence and distribution of metal-reducing microorganisms in petroleum
reservoirs. The research focused on the isolation, characterisation and identification of
anaerobic bacteria from petroleum reservoirs that were capable of reducing metals and
the potential roles of these isolates in the microbial ecology and biogeochemical cycling
of petroleum reservoirs.
Petroleum reservoirs were selected for this study on the basis of physio-chemical
conditions such as temperature, salinity, pH and the presence of organic and inorganic
compounds, that were likely to provide a suitable environment for anaerobic bacteria
capable of reducing metals. Factors such as the stratigraphic features of the
sedimentary basin, age of reservoir and past oil field practices also were considered in
choosing the reservoir for study. Seven petroleum reservoirs in the USA and
Azerbaijan were chosen for extensive investigations. The physico-chemical conditions
in these reservoirs varied substantially.
A systematic study of the production water from these petroleum reservoirs revealed a
consistent presence of iron- and manganese-reducing microorganisms. It was found
that salinity and temperature play a significant and defining role in the occurrence and
distribution of these metal-reducing microorganisms. Biotic metal reduction was
detected from production waters from all but one of the oil wells sampled. It was
significant that the water from this well (Neftcala #1074) was the most saline (78 g/l
NaCI). Metal-reducing activity was detected at temperatures up to 70°C.
Two pure cultures, strains RED1 for Redwash petroleum reservoir (USA) and NEF1
from the Neftcala petroleum reservoir (Azerbaijan) were isolated and characterized.
The strains had diverse physiological and metabolic properties including the ability to
oxidize a wide range of carbon compounds and reduce a variety of metals. Their
temperature, salinity and pH optima varied markedly. Phylogenetic analyses of the 16S
rRNA of strain RED1 showed that the strain represented a new species of a new genus
in the domain Bacteria. The bacterium most closely related to strain RED1 is the
fermentative Fe(III)-reducer, Pelobacter acetylenicus (similarity value, 92.8%). Strain
NEF1 possesses a unique combination of phenotypic traits and a low mol % G+C.
From preliminary analyses and comparative biochemistry, NEF1 appears to be a novel
metal-reducing bacterium of the Flexistipes group.
The bacteria isolated in this study were able to grow at temperatures and salinities
consistent with the reservoir from which they were isolated. This indicated that
petroleum reservoirs are a new source of physiologically diverse, novel, metal-reducing
microorganisms. The bacteria isolated also demonstrated a number of characteristics
that would enable them to survive and persist in extreme subsurface conditions and
develop a selective ecological advantage in petroleum reservoir environments.
Significantly, the metal-reducing bacteria isolated were able to utilize an array of
metabolic products produced by bacteria indigenous to petroleum reservoirs. This has
resulted in a new proposed model for the ecological succession of bacteria in petroleum
reservoirs.
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Chemoporoelastic solution of transversely isotropic saturated porous mediaPerez, Arturo Diaz. January 1900 (has links) (PDF)
Thesis (Ph.D.)--University of Oklahoma, 2004. / Title from title screen (viewed on Dec. 7, 2007). Title from document title page. Includes bibliographical references. Available in PDF format via the World Wide Web.
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Oil recovery by spontaneous imbibition for a wide range of viscosity ratiosFischer, Herbert. January 2006 (has links)
Thesis (Ph. D.)--University of Wyoming, 2006. / Title from PDF title page (viewed on Dec. 20, 2007). Includes bibliographical references (p. 208-216).
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Log-linear models of petroleum product demand : an international studyHeide, Ross J. 07 1900 (has links)
No description available.
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905 |
Estimating the effect of future oil prices on petroleum engineering project investment yardsticks.Mendjoge, Ashish V 30 September 2004 (has links)
This study proposes two methods, (1) a probabilistic method based on historical oil prices and (2) a method based on Gaussian simulation, to model future prices of oil. With these methods to model future oil prices, we can calculate the ranges of uncertainty in traditional probability indicators based on cash flow analysis, such as net present values, net present value to investment ratio and internal rate of return. We found that conventional methods used to quantify uncertainty which use high, low and base prices produce uncertainty ranges far narrower than those observed historically. These methods fail because they do not capture the "shocks" in oil prices that arise from geopolitical events or supply-demand imbalances. Quantifying uncertainty is becoming increasingly important in the petroleum industry as many current investment opportunities in reservoir development require large investments, many in harsh exploration environments, with intensive technology requirements. Insight into the range of uncertainty, particularly for downside, may influence our investment decision in these difficult areas.
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Transport of carbon nanomaterials in natural rocks and their application in oilfield explorationJanuary 2012 (has links)
This report studies the application of carbon nanomaterials as a novel type of tracer in detection of residual oil. The carbon nanomaterials studied include oxidized carbon black (OCB) coated with different molecular weight polyvinyl alcohols(PVAs). Transport studies are conducted using columns packed with ground core materials, with synthetic seawater as the carrying fluid. Compared to lower molecular weight PVA-functionalized OCBs, the breakthrough of PVA(50K)-OCBs is less sensitive to aging and temperature; therefore, PVA(50K)-OCBs are chosen as nanoreporters to sequester chemical tags. Two different tags, 14 C labeled 2,2',5,5'-tetrachlorobiphenyl(PCB) and triphenylamine, are tested in the experiments. Efficient transport of tags through oil-field rocks and selective release when rocks contain oil are demonstrated. The kinetics of PCB adsorption is studied to better understand correlation between PCB release and oil content. A linear relationship between residual oil content and PCB release is found in flow-through experiments.
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Fouling characteristics of a desalted crude oilLin, Dah-cheng 24 August 1990 (has links)
The fouling characteristics of a desalted crude oil were investigated in a systematic
investigation. There are two main parts in this study, the dry bulk tests (dehydrated crude
oil) and the wet bulk tests (to which desalter brine was added). Three barrels of desalted
crude oil provided by Amoco Oil Company were studied.
For the dry bulk tests, no brine was added to the crude oil. The effects of fluid
velocity and surface temperature on fouling were investigated. The higher the surface
temperature the greater the fouling was observed. Fouling decreased with an increase of
fluid velocity. Fluid velocity had a stronger effect on fouling at low surface temperatures
than at high surface temperatures. It was also observed that the fouling behavior of crude
oil depended on small difference in composition. The threshold surface temperatures for
the initiation of fouling were 400-450 °F (3.0 ft/sec), 525-550 °F (5.5 ft/sec), 550-600
°F (8.0 ft/sec) and about 600 °F (10.0 ft/sec) for Barrel No. 2 and Barrel No. 3. For
Barrel No. 1 however, the threshold surface temperatures were about 550 °F (3.0 ft/sec)
and 600 °F (5.5 ft/sec).
For the wet bulk tests, a certain amount desalter brine (weight percentage = 0.8%)
was added to the crude oil for each run. The effects of fluid velocity, surface temperature
and the presence of brine on fouling were investigated. Higher surface temperature
enhanced fouling considerably. Fouling was reduced as fluid velocity was increased. It
was shown that brine had a strong effect on fouling. No fouling occurred for velocities of
5.5 and 8.0 ft/sec at a surface temperature of 350 °F which was a condition for which an
aqueous phase was present and the salt remained in solution. Significant fouling occurred
for velocities of 5.5 and 8.0 ft/sec at a surface temperature operated at a low 400 °F (Tb =
300 °F) which was a condition for which the aqueous phase at the heat transfer surface was
dissolved or boiled to extinction and the salt was deposited on the heat transfer surface. / Graduation date: 1991
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The Fates of Vanadium and Sulfur Introduced with Petcoke to Lime KilnsFan, Xiaofei 31 December 2010 (has links)
Petroleum coke (petcoke) has been burned at kraft pulp mills to partially substitute for
natural gas and fuel oil used in lime kilns. Due to the high vanadium and sulfur contents in petcoke, there had been concerns over the impact of burning petcoke on kiln and chemical recovery operations. Laboratory studies were performed to examine the fate of vanadium and sulfur in lime kilns and chemical recovery cycle. The results suggest that most of the vanadium in petcoke quickly forms calcium vanadates with lime in the kiln, mostly 3CaO•V2O5. In the causticizers, calcium vanadates react with Na2CO3 in green liquor to form sodium vanadate (NaVO3). Due to its high solubility, NaVO3 dissolves in the liquor circulating around the chemical recovery system. V becomes enriched in the liquor, leading to vanadium build-up in the system. The S in petcoke would stay in the reburned lime, lower the lime availability, increase SO2 emissions from the kiln stack, alter the S balance, increase the liquor sulphidity, and potentially contribute to ring formation in the kiln.
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The Fates of Vanadium and Sulfur Introduced with Petcoke to Lime KilnsFan, Xiaofei 31 December 2010 (has links)
Petroleum coke (petcoke) has been burned at kraft pulp mills to partially substitute for
natural gas and fuel oil used in lime kilns. Due to the high vanadium and sulfur contents in petcoke, there had been concerns over the impact of burning petcoke on kiln and chemical recovery operations. Laboratory studies were performed to examine the fate of vanadium and sulfur in lime kilns and chemical recovery cycle. The results suggest that most of the vanadium in petcoke quickly forms calcium vanadates with lime in the kiln, mostly 3CaO•V2O5. In the causticizers, calcium vanadates react with Na2CO3 in green liquor to form sodium vanadate (NaVO3). Due to its high solubility, NaVO3 dissolves in the liquor circulating around the chemical recovery system. V becomes enriched in the liquor, leading to vanadium build-up in the system. The S in petcoke would stay in the reburned lime, lower the lime availability, increase SO2 emissions from the kiln stack, alter the S balance, increase the liquor sulphidity, and potentially contribute to ring formation in the kiln.
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Dual gradient drilling simulationsSigurjonsson, Kjartan Örn January 2012 (has links)
The system studied in this thesis is called the Low Rise Return system and uses a partly filled marine drilling riser with a variable mud level which is used control the bottom holes pressure.Initially main components of the Low Riser Return System are listed and explained. Then the performance characteristics of the system are explored. Level movements in riser during level increase and decrease at constant mud pump rates are explained along with the effect of mud pump rate on maximum level increase and decrease rates.A simple simulator is then presented that calculates the bottom hole pressure when pump rates are changed. The simulator includes a function that enables it to simulate lost circulation scenarios.The simulator is used to simulate some preferred scenarios. First a pressure increase and decrease at constant mud pump rates are simulated. Then it is shown how a faster pressure decrease can be achieved by temporarily lowering the mud pump rate. Next simulations are shown where changes in mud level are used to compensate for changes in equivalent circulation density as mud pump rates are changed. Finally simulations are run that demonstrate how mud level can be reduced to cure lost circulation scenarios. Results and lessons learned are then discussed.
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