28 research outputs found
Performance and emissions characteristics of a direct injection diesel engine from compressing producer gas in a dual fuel mode
This research highlights the impact of compressed producer gas combined with diesel fuel in a dual fuel mode on performance and emission characteristics of a three-cylinder diesel engine connected to an AC generator. Producer gas was generated from a small downdraft gasifier using charcoal, and sent into the engine using a supercharger to increase the gas flow rate from 76 to 125 lpm. The engine speed was adjusted from 1,000 to 1,600 rpm, while operating at full load. All results of this investigation indicate that supercharging producer gas improved the diesel economy and engine performance characteristics, but it increased the amount of various pollutants. Engine performance testing results from compressing producer gas showed that the use of gas flow rates of 116 to 125 lpm increased the maximum diesel saving by 41%, electrical power by 1.88%, and thermal efficiency by 35.76% as compared to a diesel fuel only mode. Additionally, specific energy consumption decreased with increasing producer gas flow rate and engine speed. For measuring the emissions of the engine, exhaust gas temperature increased from 223 to 276 oC, CO2 emissions increased from 21.59 to 33.90%, CO emissions increased from 0.36 to 0.59%, HC emissions increased from 23 to 58 ppm, and smoke opacity increased from 4.00 to 6.07 K.m-1 compared with the diesel fuel only mode
Forced Convection Heat Transfer from a Finite-Height Cylinder
[EN] This paper presents a large eddy simulation of forced convection heat transfer in
the flow around a surface-mounted finite-height circular cylinder. The study was carried out
for a cylinder with height-to-diameter ratio of 2.5, a Reynolds number based on the cylinder
diameter of 44 000 and a Prandtl number of 1. Only the surface of the cylinder is heated
while the bottom wall and the inflow are kept at a lower fixed temperature. The approach
flow boundary layer had a thickness of about 10% of the cylinder height. Local and averaged
heat transfer coefficients are presented. The heat transfer coefficient is strongly affected
by the free-end of the cylinder. As a result of the flow over the top being downwashed
behind the cylinder, a vortex-shedding process does not occur in the upper part, leading
to a lower value of the local heat transfer coefficient in that region. In the lower region,
vortex-shedding takes place leading to higher values of the local heat transfer coefficient.
The circumferentially averaged heat transfer coefficient is 20 % higher near the ground than
near the top of the cylinder. The spreading and dilution of the mean temperature field in the
wake of the cylinder are also discussed.The simulation was carried out using the supercomputing facilities of the Steinbuch Centre for Computing (SCC) of the Karlsruhe Institute of Technology. MGV has been partially supported by grant TRA2012-37714 of the Spanish Ministry of Economy and Competitiveness.GarcĂa Villalba, M.; Palau-Salvador, G.; Rodi, W. (2014). Forced Convection Heat Transfer from a Finite-Height Cylinder. Flow, Turbulence and Combustion. 93(1):171-187. https://doi.org/10.1007/s10494-014-9543-7S171187931Ames, F., Dvorak, L.: Turbulent transport in pin fin arrays: experimental data and predictions. J. Turbomach. 128(1), 71â81 (2006)Armstrong, J., Winstanley, D.: A review of staggered array pin fin heat transfer for turbine cooling applications. J. Turbomach. 110, 94 (1988)Breuer, M., Rodi, W.: Large eddy simulation of complex turbulent flows of practical interest. In: Hirschel, E. (ed.) Flow Simulation with High Performance Computers II, Notes on Numerical Fluid Mechanics, Vol. 52, pp 258â274. Vieweg, Braunschweig (1996)Chen, S., Sanitjai, S., Ghosh, K., Goldstein, R.: Three-dimensional vortex flow near the endwall of a short cylinder in crossflow: uniform-diameter circular cylinder. Appl. Therm. Eng. 49, 73â78 (2012)Delibra, G., Hanjalic, K., Borello, D., Rispoli, F.: Vortex structures and heat transfer in a wall-bounded pin matrix: LES with a RANS wall-treatment. Int. J. Heat Fluid Flow 31(5), 740â753 (2010)Denev, J.A., Fröhlich, J., Bockhorn, H.: Large eddy simulation of a swirling transverse jet into a crossflow with investigation of scalar transport. Phys. Fluids 21, 015101 (2009)Donnert, G.D., Kappler, M., Rodi, W.: Measurement of tracer concentration in the flow around finite-height cylinders. J. Turbul. 8, 33 (2007)Frederich, O., Thiele, F.: Turbulent flow dynamics caused by a truncated cylinder. Int. J. Heat Fluid Flow 32(3), 546â557 (2011)Fröhlich, J., GarcĂa-Villalba, M., Rodi, W.: Scalar mixing and largeâscale coherent structures in a turbulent swirling jet. Flow Turbul. Combust. 80, 47â59 (2008)Fröhlich, J., Rodi, W.: LES of the flow around a cylinder of finite height. Int. J. Heat Fluid Flow 25, 537â548 (2004)GarcĂa-Villalba, M., Fröhlich, J.: LES of a free annular swirling jetâDependence of coherent structures on a pilot jet and the level of swirl. Int. J. Heat Fluid Flow 27(5), 911â923 (2006)GarcĂa-Villalba, M., Li, N., Rodi, W., Leschziner, M.A.: Large eddy simulation of separated flow over a three-dimensional axisymmetric hill. J. Fluid Mech. 627, 55â96 (2009)Germano, M., Piomelli, U., Moin, P., Cabot, W.: A dynamic subgrid-scale eddy viscosity model. Phys. Fluids 3, 1760â1765 (1991)Hinckel, J.N., Nagamatsu, H.T.: Heat transfer in the stagnation region of the junction of a circular cylinder perpendicular to a flat plate. Int. J. Heat Mass Tran. 29(7), 999â1005 (1986)Hinterberger, C.: Dreidimensionale und tiefengemittelte Large-eddy-simulation von flachwasserströmungen. University of Karlsruhe (2004). Ph.D. thesisHölscher, N., Niemann, H.J.: Some aspects about the flow around a surface-mounted circular cylinder in a turbulent shear flow. In: Proceedings of 6th Symp. Int. Turbulent Shear Flows, ToulouseKrajnovic, S.: Flow around a tall finite cylinder explored by large eddy simulation. J. Fluid Mech. 676, 294â317 (2011)Lilly, D.: A proposed modification of the Germano subgrid-scale closure method. Phys. Fluids 4, 633â635 (1992)Morgan, V.T.: The overall convective heat transfer from smooth circular cylinders. Adv. Heat Tran. 11, 199â264 (1975)NiÄeno, B., Dronkers, A., HanjaliÄ, K.: Turbulent heat transfer from a multi-layered wall-mounted cube matrix: a large eddy simulation. Int. J. Heat Fluid Flow 23(2), 173â185 (2002)Palau-Salvador, G., GarcĂa-Villalba, M., Rodi, W.: Scalar transport from point sources in the flow around a finite-height cylinder. Environ. Fluid Mech. 11, 611â625 (2011)Palau-Salvador, G., Stoesser, T., Fröhlich, J., Kappler, M., Rodi, W.: Large-eddy simulations and experiments of flow around finite-height cylinders. Flow Turbul. Combust. 84, 239â275 (2010)Pattenden, R., Turnock, S., Zhang, X.: Measurements of the flow over a low-aspect ratio cylinder mounted on a ground plate. Exp. Fluids 39, 10â21 (2005)Pierce, C.: Progress-variable approach for large-eddy simulation of turbulent combustion. Stanford University (2001). Ph.D. thesisPopovac, M., Hanjalic, K.: Vortices and heat flux around a wall-mounted cube cooled simultaneously by a jet and a crossflow. Int. J. Heat Mass Transfer 52, 4047â4062 (2009)Rhie, C., Chow, W.: Numerical study of the turbulent flow past an airfoil with trailing edge separation. AIAA J. 21(11), 1061â1068 (1983)Rostamy, N., Sumner, D., Bergstrom, D.J., Bugg, J.D.: Local flow field of a surface-mounted finite circular cylinder. J. Fluids Struct. 34, 105â122 (2012)Sanitjai, S., Goldstein, R.J.: Forced convection heat transfer from a circular cylinder in crossflow to air and liquids. Int. J. Heat Mass Tran 47, 4795â4805 (2004)Sanitjai, S., Goldstein, R.J.: Heat transfer from a circular cylinder to mixtures of water and ethylene glycol. Int. J. Heat Mass Tran. 47, 4785â4794 (2004)Sparrow, E.M., Stahl, T.J., Traub, P.: Heat transfer adjacent to the attached end of a cylinder in crossflow. Int. J. Heat Mass Tran. 27(2), 233â242 (1984)Stone, H.: Iterative solution of implicit approximations of multidimensional partial differential equations for finite difference Methods. SIAM J. Numer. Anal. 5, 530â558 (1968)Sumner, D.: Flow above the free end of a surface-mounted finite-height circular cylinder: a review. J. Fluids Struct. 43, 41â63 (2013)Tsutsui, T., Igarashi, T., Nakamura, H.: Fluid flow and heat transfer around a cylindrical protuberance mounted on a flat plate boundary layer. JSME Ser. B 43(2), 279â287 (2000)Tsutsui, T., Kawahara, M.: Heat transfer around a cylindrical protuberance mounted in a plane turbulent boundary layer. J. Heat Tran. 128, 153â161 (2006)Tutar, M., Akkoca, A.: Numerical analysis of fluid flow and heat transfer characteristics in three-dimensional plate fin-and-tube heat exchangers. Num. Heat Tran. A 46, 301â321 (2004)Zhu, J.: Low diffusive and oscillationâfree convection scheme. Comm. Appl. Num. Meth. 7, 225â232 (1991)Zukauskas, A.A.: Heat transfer from tubes in cross-flow. Adv. Heat Tran. 8, 93â160 (1972
Satellite image analysis and frozen cylinder experiments on thermal erosion of periglacial fluvial islands
International audienceFrozen islands in the Lena River, Siberia, experience rates of fluvial thermal erosion exceeding 10m/year. The islands erode differentially, with rates of frontal retreat exceeding those on island sides. We define the erosion ratio (ER) between the front and sides to estimate this differential erosion. A GISâbased study of 19 islands from 1967 to 2010 indicated average erosion rates of 19.7 and 3.7 m/year for the island heads and sides, respectively. The average ER over the period was 4.7. An analytical model of local thermal erosion for a frozen cylinder of sand in a turbulent water flow is proposed, assuming an ablation process. Thermal erosion of 19 frozen cylinders was measured for water flows of different temperature and velocity in a cold chamber. As observed in the field, frontal erosion always exceeded lateral erosion, with an average ER of 1.6. The ER decreased with increasing temperature from 5 to 15°C. The higher value of ER in the field may be due to interactions with neighboring islands and banks. An empirical law including phase change and the process of erosion is proposed, and validates our model compared with previous laws that do not account for erosion. The erosion process enhances heat transfer
Forced convection and heat transfer around a bounded cylinder
The article deals with the heat transfer solution in the fluid flow inside a pipe, the small tube is inserted into the pipe and its axis is perpendicular to the axis of the pipe. The fluid is water, the regime of the fluid flow is turbulent. The small tube is loaded by the internal source of the heat, the power of the source is constant and homogenous over the small tube surface and the cold water cools down the small tube. The analysis of the described problem helps to design the experimental model (the heat source above all) to validate the CFD results. The work included the numeric and analytic method. The model was prepared with the aim to investigate large amount of the variants of the geometric set up (the tube and pipe diameters ratio, the geometrical aspect ratio, corresponding stabilization length of the pipe for given diameter), the flow properties (variation of the velocity values, Reynolds number) and the power of the heat source (ensuring the measurable differences of the temperatures on the tube surface, large Nusselt number). The effect of the constrained space has been observed and described, compare to the free fluid flow