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    , COMPUTERS & CHEMICAL ENGINEERING, Vol: 74, Pages: 169-183, ISSN: 0098-1354
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    , INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, Vol: 54, Pages: 8587-8599, ISSN: 0888-5885
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    , FLUID PHASE EQUILIBRIA, Vol: 365, Pages: 20-40, ISSN: 0378-3812
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    , JOURNAL OF PHYSICAL CHEMISTRY B, Vol: 118, Pages: 14461-14478, ISSN: 1520-6106
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    Advanced reservoir characterization for CO<inf>2</inf> storage

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    next launcher 3d full cracked Injection of CO2 into the subsurface is of interest for CO 2 storage and enhanced oil recovery (EOR). There are, however, major unresolved questions around the multiphase flow physics and reactive processes that will take place after CO2 is injected, particularly in carbonate rock reservoirs. For example, the wetting properties of CO2-brine- rock systems will impact the efficiency of EOR operations and CO2 storage but reported contact angles range widely from strongly water-wet to intermediate wet. Similar uncertainties exist for properties including the relative permeability and the impact of chemical reaction on flow. In this presentation we present initial results from laboratory studies investigating the physics of multiphase flow and reactive transport for CO2-brine systems. We use traditional and novel core flooding techniques and x-ray imaging to resolve uncertainties around the CO2-brine contact angle, relative permeability, residual trapping, and feedbacks between chemical reaction and flow in carbonate rocks. Copyright 2014, International Petroleum Technology Conference.

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    , RHEOLOGICA ACTA, Vol: 53, Pages: 373-384, ISSN: 0035-4511
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    , ENERGY & ENVIRONMENTAL SCIENCE, Vol: 7, Pages: 130-189, ISSN: 1754-5692
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    , 12th International Conference on Greenhouse Gas Control Technologies (GHGT), Publisher: ELSEVIER SCIENCE BV, Pages: 2622-2629, ISSN: 1876-6102
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    , Green Chemistry, Vol: 16, Pages: 3098-3106, ISSN: 1744-1560

    dvd fab crack Through more than two decades’ intensive research, ionic liquids (ILs) have exhibited significant potential in various areas of research at laboratory scales. This suggests that ILs-based industrial process development will attract increasing attention in the future. However, there is one core issue that stands in the way of commercialisation: the high cost of most laboratory-synthesized ILs will limit application to small-scale, specialized processes. In this work, we evaluate the economic feasibility of two ILs synthesized via acid–base neutralization using two scenarios for each: conventional and intensification processing. Based upon our initial models, we determined the cost price of each IL and compared the energy requirements of each process option. The cost prices of triethylammonium hydrogen sulfate and 1-methylimidazolium hydrogen sulfate are estimated as $1.24 kg−1 and $2.96–5.88 kg−1, respectively. This compares favourably with organic solvents such as acetone or ethyl acetate, which sell for $1.30–$1.40 kg−1. Moreover, the raw materials contribute the overwhelming majority of this cost and the intensified process using a compact plate reactor is more economical due to lower energy requirements. These results indicate that ionic liquids are not necessarily expensive, and therefore large-scale IL-based processes can become a commercial reality.

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    , FLUID PHASE EQUILIBRIA, Vol: 363, Pages: 239-247, ISSN: 0378-3812
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    , Handbook of Sustainable Development: Second Edition, Pages: 532-550, ISBN: 9781782544708
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    , IEEE TRANSACTIONS ON ENGINEERING MANAGEMENT, Vol: 61, Pages: 251-260, ISSN: 0018-9391
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    The Impact of Government Interventions on Investment in the GB Electricity Market

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    , 12th International Conference on Greenhouse Gas Control Technologies (GHGT), Publisher: ELSEVIER SCIENCE BV, Pages: 7494-7507, ISSN: 1876-6102
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    , JOURNAL OF PHYSICAL CHEMISTRY B, Vol: 118, Pages: 6206-6221, ISSN: 1520-6106
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    , International Journal of Greenhouse Gas Control, Vol: 27, Pages: 103-119, ISSN: 1750-5836

    soy un crack del futbol We present a model of a coal-fired power plant integrated with a dynamic model of a monoethanolamine (MEA)-based post-combustion CO₂ capture process. We evaluate base- and part-load operating modes of the integrated power and CO₂ capture plant. We propose a simple modification to the base-process which exploits the tradeoff between thermodynamic and rate or kinetic driving forces for mass transfer. This modification returns a portion of the regenerated solvent to the middle of the absorption column at an elevated temperature. Under base-load operation of the power plant, this modification was observed to increase the degree of CO₂ capture by 9.9% and reduce the reboiler duty by 8.3%, improving the net electrical efficiency of the decarbonised power plant from 28.27% to 29.15% - a relative increase of 2.8%. Under part-load operation, the degree of CO₂ capture increased by 1% with a concurrent reduction in reboiler duty of 16.7% and an increase in overall process efficiency of 3.25%

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    , 12th International Conference on Greenhouse Gas Control Technologies (GHGT), Publisher: ELSEVIER SCIENCE BV, Pages: 1525-1535, ISSN: 1876-6102
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    , ENERGY & FUELS, Vol: 28, Pages: 1028-1040, ISSN: 0887-0624
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    , RENEWABLE & SUSTAINABLE ENERGY REVIEWS, Vol: 30, Pages: 616-640, ISSN: 1364-0321
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    The impact of reservoir conditions on the measurement of multiphase flow properties for CO2-brine systems

    , Pages: 77-81

    activation keygen for microsoft office 2013 Successful industrial scale carbon dioxide injection into deep saline aquifers will be dependent on the ability to model the flow of the fluid and to quantify the impact of various trapping mechanisms. The effectiveness of the models is in turn dependent on high quality laboratory measurements ofbasic multiphase flow properties such as relative permeability and residual trapping at reservoir conditions. At the same time there exists general uncertainty around the few existing published data on these properties for CO2-brine systems. In this study we present results from a newly constructed reservoir condition coreflooding and imaging laboratory designed to measure multiphase flow properties, capillary pressure, relative permeability and residual trapping at a range of reservoir conditions. The proper approach to measuring relative permeability for CO2-brine system is proposed and demonstrated. The changes in residual trapping correlated to pressure, temperature, brine salinity, interfacial tension, and contact angle are also reported. We also show with a combination of simulations of corefloods and experiments performed at various conditions that high precision results can be obtained for this system when the appropriate conditions are used. Copyright © (2014) by the European Association of Geoscientists & Engineers. All rights reserved.

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    , ENERGY POLICY, Vol: 73, Pages: 298-311, ISSN: 0301-4215
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    , COMPUTERS & INDUSTRIAL ENGINEERING, Vol: 74, Pages: 68-83, ISSN: 0360-8352
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    , GHGT-11, Vol: 37, Pages: 2552-2561, ISSN: 1876-6102
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    , BIOMASS & BIOENERGY, Vol: 58, Pages: 31-51, ISSN: 0961-9534
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    The Future Role of Energy in Manufacturing

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    , ENERGY POLICY, Vol: 63, Pages: 55-68, ISSN: 0301-4215
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    , International Conference on Greenhouse Gas Technologies (GHGT), Publisher: ELSEVIER SCIENCE BV, Pages: 4499-4503, ISSN: 1876-6102

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