The Mechanics of Shallow Magma Reservoir Outgassing
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Stall/Surge Dynamics of a Multi-Stage Air Compressor in Response to a Load Transient of a Hybrid Solid Oxide Fuel Cell-Gas Turbine System
Journal of Power Sources 365 (2017) 408e418 Contents lists available at ScienceDirect Journal of Power Sources journal homepage: www.elsevier.com/locate/jpowsour Stall/surge dynamics of a multi-stage air compressor in response to a load transient of a hybrid solid oxide fuel cell-gas turbine system * Mohammad Ali Azizi, Jacob Brouwer Advanced Power and Energy Program, University of California, Irvine, USA highlights Dynamic operation of a hybrid solid oxide fuel cell gas turbine system was explored. Computational fluid dynamic simulations of a multi-stage compressor were accomplished. Stall/surge dynamics in response to a pressure perturbation were evaluated. The multi-stage radial compressor was found robust to the pressure dynamics studied. Air flow was maintained positive without entering into severe deep surge conditions. article info abstract Article history: A better understanding of turbulent unsteady flows in gas turbine systems is necessary to design and Received 14 August 2017 control compressors for hybrid fuel cell-gas turbine systems. Compressor stall/surge analysis for a 4 MW Accepted 4 September 2017 hybrid solid oxide fuel cell-gas turbine system for locomotive applications is performed based upon a 1.7 MW multi-stage air compressor. Control strategies are applied to prevent operation of the hybrid SOFC-GT beyond the stall/surge lines of the compressor. Computational fluid dynamics tools are used to Keywords: simulate the flow distribution and instabilities near the stall/surge line. The results show that a 1.7 MW Solid oxide fuel cell system compressor like that of a Kawasaki gas turbine is an appropriate choice among the industrial Hybrid fuel cell gas turbine Dynamic simulation compressors to be used in a 4 MW locomotive SOFC-GT with topping cycle design. -
CFD Based Design for Ejector Cooling System Using HFOS (1234Ze(E) and 1234Yf)
energies Article CFD Based Design for Ejector Cooling System Using HFOS (1234ze(E) and 1234yf) Anas F A Elbarghthi 1,*, Saleh Mohamed 2, Van Vu Nguyen 1 and Vaclav Dvorak 1 1 Department of Applied Mechanics, Faculty of Mechanical Engineering, Technical University of Liberec, Studentská 1402/2, 46117 Liberec, Czech Republic; [email protected] (V.V.N.); [email protected] (V.D.) 2 Department of Mechanical and Materials Engineering, Masdar Institute, Khalifa University of Science and Technology, Abu Dhabi, UAE; [email protected] * Correspondence: [email protected] Received: 18 February 2020; Accepted: 14 March 2020; Published: 18 March 2020 Abstract: The field of computational fluid dynamics has been rekindled by recent researchers to unleash this powerful tool to predict the ejector design, as well as to analyse and improve its performance. In this paper, CFD simulation was conducted to model a 2-D axisymmetric supersonic ejector using NIST real gas model integrated in ANSYS Fluent to probe the physical insight and consistent with accurate solutions. HFOs (1234ze(E) and 1234yf) were used as working fluids for their promising alternatives, low global warming potential (GWP), and adhering to EU Council regulations. The impact of different operating conditions, performance maps, and the Pareto frontier performance approach were investigated. The expansion ratio of both refrigerants has been accomplished in linear relationship using their critical compression ratio within 0.30% accuracy. The results show that ± R1234yf achieved reasonably better overall performance than R1234ze(E). Generally, by increasing the primary flow inlet saturation temperature and pressure, the entrainment ratio will be lower, and this allows for a higher critical operating back pressure. -
Formation of the Lower Ocean Crust and the Crystallization of Gabbroic Cumulates at a Very Slowly Spreading Ridge
Journal of Volcanology and Geothermal Research 110 ?2001) 191±233 www.elsevier.com/locate/jvolgeores Formation of the lower ocean crust and the crystallization of gabbroic cumulates at a very slowly spreading ridge James H. Natlanda,*, Henry J.B. Dickb aRosenstiel School of Marine and Atmospheric Science, University of Miami, Miami, FL 33149, USA bWoods hole Oceanographic Institution, Woods hole, MA 02543, USA Revised 25 June 2000 Abstract Ocean Drilling Program Hole 735B was extended to 1508 m below the sea ¯oor during Leg 176, atop a shallow banknear Atlantis II Fracture Zone on the very slowly spreading Southwest Indian Ridge. All the drilling was in gabbro, and recovery averaged nearly 87%. The drill penetrated a series of stacked plutons consisting mostly of olivine gabbro, but some with troctolite. Each pluton is some 200±500 m thick, each has its own internally coherent stratigraphy, and each apparently represents an individual event of signi®cant magma in¯ation and addition to the crust. The entire column was extensively deformed along inclined zones of distributed shear before it was completely frozen, this marking the onset of unroo®ng of the rocks and their ascent to high rift mountains. The deformation mobilized late-stage melts into ¯ow patterns which led to concentration of ilmenite and magnetite in hundreds of seams of oxide gabbro along or near zones of strong crystal±plastic deformation, the highly differentiated melts overall being concentrated by buoyancy forces toward the top of the section, especially in one zone nearly 70 m thick. However, upward ¯ow was ultimately blocked or de¯ected by zones of impermeable rockresulting either from downward freezing or grain-size reduction during shear. -
MSME with Depth in Fluid Mechanics
MSME with depth in Fluid Mechanics The primary areas of fluid mechanics research at Michigan State University's Mechanical Engineering program are in developing computational methods for the prediction of complex flows, in devising experimental methods of measurement, and in applying them to improve understanding of fluid-flow phenomena. Theoretical fluid dynamics courses provide a foundation for this research as well as for related studies in areas such as combustion, heat transfer, thermal power engineering, materials processing, bioengineering and in aspects of manufacturing engineering. MS Track for Fluid Mechanics The MSME degree program for fluid mechanics is based around two graduate-level foundation courses offered through the Department of Mechanical Engineering (ME). These courses are ME 830 Fluid Mechanics I Fall ME 840 Computational Fluid Mechanics and Heat Transfer Spring The ME 830 course is the basic graduate level course in the continuum theory of fluid mechanics that all students should take. In the ME 840 course, the theoretical understanding gained in ME 830 is supplemented with material on numerical methods, discretization of equations, and stability constraints appropriate for developing and using computational methods of solution to fluid mechanics and convective heat transfer problems. Students augment these courses with additional courses in fluid mechanics and satisfy breadth requirements by selecting courses in the areas of Thermal Sciences, Mechanical and Dynamical Systems, and Solid and Structural Mechanics. Graduate Course and Research Topics (Profs. Benard, Brereton, Jaberi, Koochesfahani, Naguib) ExperimentalResearch Many fluid flow phenomena are too complicated to be understood fully or predicted accurately by either theory or computational methods. Sometimes the boundary conditions of real-world problems cannot be analyzed accurately. -
Small Volume Andesite Magmas and Melt–Mush Interactions at Ruapehu, New Zealand: Evidence from Melt Inclusions
Contrib Mineral Petrol DOI 10.1007/s00410-013-0880-7 ORIGINAL PAPER Small volume andesite magmas and melt–mush interactions at Ruapehu, New Zealand: evidence from melt inclusions Geoff Kilgour • Jon Blundy • Kathy Cashman • Heidy M. Mader Received: 1 November 2012 / Accepted: 12 April 2013 Ó Springer-Verlag Berlin Heidelberg 2013 Abstract Historical eruptions from Mt. Ruapehu (New From these data, we infer that individual melt batches rise Zealand) have been small (\0.001 km3 of juvenile magma) through, and interact with, crystal mush zones formed by and have often occurred without significant warning. antecedent magmas. From this perspective, we envision the Developing better modelling tools requires an improved magmatic system at Ruapehu as frequently recharged by understanding of the magma storage and transport system small magma inputs that, in turn, cool and crystallise to beneath the volcano. Towards that end, we have analysed varying degrees. Melts that are able to erupt through this the volatile content and major element chemistry of network of crystal mush entrain (to a greater or lesser groundmass glass and phenocryst-hosted melt inclusions in extent) exotic crystals. In the extreme case (such as the 1996 erupted samples from 1945 to 1996. We find that during this eruption), the resulting scoria contain melt inclusion-bear- time period, magma has been stored at depths of *2–9 km, ing crystals that are exotic to the transporting magma. consistent with inferences from geophysical data. Our data Finally, we suggest that complex interactions between also show that Ruapehu magmas are relatively H2O-poor recharge and antecedent magmas are probably common, but (\2 wt%) and CO2-rich (B1,000 ppm) compared to typical that the small volumes and short time scales of recharge at arc andesites. -
COMSOL Computational Fluid Dynamics for Microreactors Used in Volatile Organic Compounds Catalytic Elimination
COMSOL Computational Fluid Dynamics for Microreactors Used in Volatile Organic Compounds Catalytic Elimination Maria Olea 1, S. Odiba1, S. Hodgson1, A. Adgar1 1School of Science and Engineering, Teesside University, Middlesbrough, United Kingdom Abstract Volatile organic compounds (VOCs) are organic chemicals that will evaporate easily into the air at room temperature and contribute majorly to the formation of photochemical ozone. They are emitted as gases from certain solids and liquids in to the atmosphere and affect indoor and outdoor air quality. They includes acetone, benzene, ethylene glycol, formaldehyde, methylene chloride, perchloroethylene, toluene, xylene, 1,3-butadiene, butane, pentane, propane, ethanol, etc. Source of VOCs emission include paints, industrial processes, transportation activities, household products such as cleaning agents, aerosols, fuel and cosmetics. Catalytic oxidation is one of the most promising elimination techniques for VOCs as a result of it flexibility and energy saving. The catalytic materials enhance the chemical reactions that convert VOCs (through oxidation) into carbon dioxide and water. Removal of volatile organic compounds at room temperature has always been a challenge to researchers. Developing a catalyst which could completely oxidize the VOCs at very low temperature in order to avoid catalyst deactivation and promote energy saving has been the key focus among researchers in the recent years. Moreover, as the oxidation reaction is highly exothermic, the use of catalytic microreactors instead of packed bed reactors was considered. Microreactors are microfabricated catalytic chemical reactors with at least one linear dimension in the micrometer range. Usually, they consist of narrow channels and exhibit large surface area-to- volume ratios which leads to high heat and mass transfer properties. -
Exsolved Volatiles in Magma Reservoirs 4 5 Marie Edmonds1* and Andrew W
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by Apollo 1 JVGR review paper 2 3 Exsolved Volatiles in Magma Reservoirs 4 5 Marie Edmonds1* and Andrew W. Woods1,2 6 7 1 Earth Sciences Department, University of Cambridge, Downing Street, Cambridge CB2 3EQ, UK 8 2 BP Institute, Bullard Laboratories, Madingley Rd, Cambridge CB3 0EZ, UK 9 10 *Corresponding author, [email protected] 11 12 1. Introduction 13 2. Achieving volatile saturation in magmas 14 2.1. Volatiles in natural magmatic systems 15 2.2. Sulfur partitioning into the exsolved volatile phase 16 3. Consequences of exsolved volatiles in magma reservoirs for rheology and dynamics 17 3.1. Magma compressibility 18 3.2. Pressure increase during second boiling 19 3.3. Effect of compressibility on the mass of magma erupted 20 4. The role of the exsolved volatile phase in magma mixing and mingling 21 4.1. Magma mixing and overturn, driven by vesiculation of the lower magma layer 22 4.2. Vesiculation of underplating magmas and formation of mafic enclaves 23 5. Exsolved volatile phase generation and transport through crystal-rich magma bodies 24 5.1. Transport of an exsolved volatile phase in crystal-rich magma 25 5.2. Implications of our new understanding of the transport of the exsolved volatile phase 26 through crystalline magmas for ore deposits 27 6. Summary and problems for the future 28 29 30 31 32 33 34 1 35 Abstract 36 We review our understanding of the exsolved volatile phase co-existing with magmas during pre- 37 eruptive storage at the pressures and temperatures corresponding to crustal magma reservoirs. -
THERMODYNAMICS, HEAT TRANSFER, and FLUID FLOW, Module 3 Fluid Flow Blank Fluid Flow TABLE of CONTENTS
Department of Energy Fundamentals Handbook THERMODYNAMICS, HEAT TRANSFER, AND FLUID FLOW, Module 3 Fluid Flow blank Fluid Flow TABLE OF CONTENTS TABLE OF CONTENTS LIST OF FIGURES .................................................. iv LIST OF TABLES ................................................... v REFERENCES ..................................................... vi OBJECTIVES ..................................................... vii CONTINUITY EQUATION ............................................ 1 Introduction .................................................. 1 Properties of Fluids ............................................. 2 Buoyancy .................................................... 2 Compressibility ................................................ 3 Relationship Between Depth and Pressure ............................. 3 Pascal’s Law .................................................. 7 Control Volume ............................................... 8 Volumetric Flow Rate ........................................... 9 Mass Flow Rate ............................................... 9 Conservation of Mass ........................................... 10 Steady-State Flow ............................................. 10 Continuity Equation ............................................ 11 Summary ................................................... 16 LAMINAR AND TURBULENT FLOW ................................... 17 Flow Regimes ................................................ 17 Laminar Flow ............................................... -
Performance Evaluation of Multipurpose Solar Heating System
Mechanics and Mechanical Engineering Vol. 20, No. 4 (2016) 359{370 ⃝c Lodz University of Technology Performance Evaluation of Multipurpose Solar Heating System R. Venkatesh Department of Mechanical Engineering Srinivasan Engineering College Perambalur, Tamilnadu, India V. Vijayan Department of Mechanical Engineering K. Ramakrishnan College of Technology Samayapuram, Trichy, Tamilnadu, India Received (29 May 2016) Revised (26 July 2016) Accepted (25 September 2016) In order to increase the heat transfer and thermal performance of solar collectors, a multipurpose solar collector is designed and investigated experimentally by combining the solar water collector and solar air collector. In this design, the storage tank of the conventional solar water collector is modified as riser tubes and header and is fitted in the bottom of the solar air heater. This paper presents the study of fluid flow and heat transfer in a multipurpose solar air heater by using Computational Fluid Dynamics (CFD) which reduces time and cost. The result reveals that in the multipurpose solar air heater at load condition, for flow rate of 0.0176 m3/s m2, the maximum average thermal efficiency was 73.06% for summer and 67.15 % for winter season. In multipurpose solar air heating system, the simulated results are compared to experimental values and the deviation falls within ± 11.61% for summer season and ± 10.64% for winter season. It proves that the simulated (CFD) results falls within the acceptable limits. Keywords: solar water collector, solar air collector, fluid flow, heat transfer and Compu- tational fluid dynamics. 1. Introduction Solar energy plays an important role in low{temperature thermal applications, since it replaces a considerable amount of conventional fuel. -
Overview of the Entropy Production of Incompressible and Compressible fluid Dynamics
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by PORTO Publications Open Repository TOrino Politecnico di Torino Porto Institutional Repository [Article] Overview of the entropy production of incompressible and compressible fluid dynamics Original Citation: Asinari, Pietro; Chiavazzo, Eliodoro (2015). Overview of the entropy production of incompressible and compressible fluid dynamics. In: MECCANICA. - ISSN 0025-6455 Availability: This version is available at : http://porto.polito.it/2624292/ since: November 2015 Publisher: Kluwer Academic Publishers Published version: DOI:10.1007/s11012-015-0284-z Terms of use: This article is made available under terms and conditions applicable to Open Access Policy Article ("Public - All rights reserved") , as described at http://porto.polito.it/terms_and_conditions. html Porto, the institutional repository of the Politecnico di Torino, is provided by the University Library and the IT-Services. The aim is to enable open access to all the world. Please share with us how this access benefits you. Your story matters. (Article begins on next page) Meccanica manuscript No. (will be inserted by the editor) Overview of the entropy production of incompressible and compressible fluid dynamics Pietro Asinari · Eliodoro Chiavazzo Received: date / Accepted: date Abstract In this paper, we present an overview of the Keywords Thermodynamics of Irreversible Processes entropy production in fluid dynamics in a systematic (TIP) · Compressible fluid dynamics · Incompress- way. First of all, we clarify a rigorous derivation of ible limit · Entropy production · Second law of the incompressible limit for the Navier-Stokes-Fourier thermodynamics system of equations based on the asymptotic analy- sis, which is a very well known mathematical technique used to derive macroscopic limits of kinetic equations 1 Introduction and motivation (Chapman-Enskog expansion and Hilbert expansion are popular methodologies). -
Durham Research Online
Durham Research Online Deposited in DRO: 14 March 2018 Version of attached le: Accepted Version Peer-review status of attached le: Peer-reviewed Citation for published item: Namur, Olivier and Humphreys, Madeleine C.S. (2018) 'Trace element constraints on the dierentiation and crystal mush solidication in the Skaergaard intrusion, Greenland.', Journal of petrology., 59 (3). pp. 387-418. Further information on publisher's website: https://doi.org/10.1093/petrology/egy032 Publisher's copyright statement: This is a pre-copyedited, author-produced version of an article accepted for publication in Journal Of Petrology following peer review. The version of record Namur, Olivier Humphreys, Madeleine C.S. (2018). Trace element constraints on the dierentiation and crystal mush solidication in the Skaergaard intrusion, Greenland. Journal of Petrology is available online at: https://doi.org/10.1093/petrology/egy032. Additional information: Use policy The full-text may be used and/or reproduced, and given to third parties in any format or medium, without prior permission or charge, for personal research or study, educational, or not-for-prot purposes provided that: • a full bibliographic reference is made to the original source • a link is made to the metadata record in DRO • the full-text is not changed in any way The full-text must not be sold in any format or medium without the formal permission of the copyright holders. Please consult the full DRO policy for further details. Durham University Library, Stockton Road, Durham DH1 3LY, United Kingdom Tel : +44 (0)191 334 3042 | Fax : +44 (0)191 334 2971 https://dro.dur.ac.uk Trace element constraints on the differentiation and crystal mush solidification in the Skaergaard intrusion, Greenland Olivier Namur1*, Madeleine C.S. -
Removal of Volatile Organic Compounds from Soil
Water Pollution X 107 Removal of volatile organic compounds from soil R. S. Amano University of Wisconsin-Milwaukee, USA Abstract Pollution by petroleum products is a source of volatile organic compounds in soil. Therefore, laboratory column venting experiments were completed in order to investigate the removal of a pure compound (toluene) and a mixture of two (toluene and n-heptane) and five (toluene, n-heptane, ethylbenzene, m-xylene and p-xylene) compounds. The choice of the compounds, as well as their proportion in the mixture, was made on the basis of the real fuel composition. The objective of this study is a comparison between the experimental volatile organic compounds removal results and the computational fluid dynamics (CFDs) analysis. The proposed model for the contaminants transport describes the removal of organic compounds from soil, the contaminants being distributed among four phases: vapor, nonaqueous liquid phase, aqueous and “solid”; the local phase’s equilibrium and the ideal behavior of all four phases was found to be accurate enough to describe the interphase mass transfer. The process developed in the lab consists of a heater/boiler that pumps and circulates hot oil through a pipeline that is enclosed in a larger-diameter pipe. This extraction pipe is vertically installed within the contaminated soil up to a certain depth and is welded at the bottom and capped at the top. The number of heat source pipes and extraction wells depends on the type of soil, the type of pollutants, and the moisture content of the soil and the size of the area to be cleaned.