... Solar drying systems: Simulations and optimization, Agrotech Publishing Academy, Udaipur, pp 131-133 Haghighi K., Segerlind L.J, (1988), Modeling Simultaneous Heat and MassTransferin Isotropic ... Trans ASEA, pp 31 Husain A., Chen C.S., Clayton J T, Whitney L.F (1972), Mathematical Simulation of Mass and Heat Transferin High Moisture Foods, Trans ASAE, pp 55-59 224 Husain A., Chen C.S., Clayton ... C.S., Clayton J T (1973), Simultaneuos Heat and Mass Diffusion in Biological Material, Trans ASAE, pp 69-73 Luikov, A V (1980), Heat and mass transfer, Mir Publisher, Moscow Peebles E D, Christopher...
... unsteady-state mass transfer, since the amount of dye in the fiber is continuously increasing Following, Equation 8, was developed by Hill for describing the diffusion of dye molecules into an infinitely ... Wesselingh, J.A., The Maxwell – Stefan approach to mass transfer, Chemical Engineering Science, 52, (1997), 861 – 911 [5] Levenspiel, O., Modeling in chemical engineering, Chemical Engineering ... in different scientific and engineering fields such as medicine, textile industry, membrane separations, packaging in food industry, extraction of solvents and of contaminants, and etc Mass transfer...
... eStudio Calamar, Berlin/Figueres Printed on acid-free paper Springer is part of Springer Science+Business Media (www.springer.com) Contents Treatment of Rising Damp in Historical Buildings ... dependant on the surface finishing materials and furnishing According to the principle, a hygroscopic inertia index was defined as a single number, representing the hygroscopic inertia of a room and that ... yielded interesting results Numerical simulation studies, using the programme WUFI-2D, have given similar findings This paper describes a new system for treating rising damp in historic buildings...
... Printed in Croatia A free online edition of this book is available at www.intechopen.com Additional hard copies can be obtained from orders@intechweb.org MassTransferin Chemical Engineering ... Wesselingh, J.A., The Maxwell – Stefan approach to mass transfer, Chemical Engineering Science, 52, (1997), 861 – 911 [5] Levenspiel, O., Modeling in chemical engineering, Chemical Engineering ... distribution of each component in oil and gas phase 13 calculating the P in the PVT cell Fig Flow chart of calculation procedure END MassTransferin Chemical Engineering Processes 3.2 Model solution...
... unsteady-state mass transfer, since the amount of dye in the fiber is continuously increasing Following, Equation 8, was developed by Hill for describing the diffusion of dye molecules into an infinitely ... in different scientific and engineering fields such as medicine, textile industry, membrane separations, packaging in food industry, extraction of solvents and of contaminants, and etc Masstransfer ... radius of filaments are presented in Fig As seen in Fig.3, decreasing in radius of filament causes increasing in the rate of saturating 1.1 1.0 0.9 0.8 ct/cinf 0.7 0.6 0.5 0.4 Radius of filament...
... walls A preliminary design of a packed column involves the following steps: Choice of packing; Column diameter estimation; 42 MassTransferin Chemical Engineering Processes Masstransfer coefficients ... surface area due to instabilities in liquid flow, such as ripples, waves, detachment of the film into liquid 56 MassTransferin Chemical Engineering Processes showers, etc The resulting correlation ... obtained during continuous operation, therefore permitting the use of the properties 60 MassTransferin Chemical Engineering Processes calculated by that software on the theoretical models investigated...
... with other researchers in the drying industry using mathematical 86 MassTransferin Chemical Engineering Processes modeling for the simulation of the drying mechanism in commercial dryers demonstrated ... structured packings Chemical Engineering and Processing, v 31, 2, pp 119 Xu, Z P., Afacan, A., Chuang, K T (2000) Predicting masstransferin packed columns containing structured packings Trans IChemE, ... mathematical formulations pertaining to the flow, heat, and masstransfer mechanisms occurring in multiphase flow systems The present numerical models for multiphase flows incorporate two approaches:...
... by convective heat and masstransfer This initial stage of drying is known as the constant or unhindered drying period (CDP) As drying proceeds, internal moisture within the particle diffuses ... geometry as shown in Figure This model discusses the drying of sludge material and linked to an earlier work presented by Jamaleddine and 100 MassTransferin Chemical Engineering Processes Ray ... drying kinetics and should be validated against experimental results This is due to the fact that model approximations are used in association with CFD 106 MassTransferin Chemical Engineering...
... pungent capsicum oleoresin, capsaicin and capsanthin with hexane 3.3.1 Model fitting The data obtained by these models demonstrated how the independent variables in the models influenced the extraction ... corrosion in the metallic parts at the interior of the engine The H2S is an inorganic acid that attacks the surface of metals when they are 134 MassTransferin Chemical Engineering Processes placed in ... (2011) Recent advances in the study on capsaicinoids and capsinoids, European Journal of Pharmacology, Vol.650, 1-7 132 MassTransferin Chemical Engineering Processes Ying-Yue, W.; Chi-Tzong,...
... concentration during bubbling tests with MEA (left) and H2S and CO2 absorbing capacity of MEA and DEA as function of their concentration in water (right) 142 MassTransferin Chemical Engineering Processes ... 1996) Electroporation is today widely used in biotechnology and medicine to deliver drugs and genes into living cells 152 MassTransferin Chemical Engineering Processes (Neumann et al., 1982; Fromm ... Cádiz, Spain 150 MassTransferin Chemical Engineering Processes Romeo, L M.; Escosa, J & Bolea, I (2006) Postcombustion CO2 sequestration, Universidad de Zaragoza, Zaragoza, Spain Steinfeld,...
... sustainable solution in this point of view In contrast to the energy-intensive interphase masstransfer processes as distillation and extraction, membrane separation is an intraphase -mass- transfer ... energy-intensive interphase masstransfer processes and less energy- or less material-intensive intraphase masstransfer processes (Henley & Seader, 1981) With environmental and energy constraints in ... located in the skin, that are only partially extracted during traditional winemaking process, due to the resistances to masstransfer of cell walls and cytoplasmatic membranes In red wine, the main...
... Transport Through HFSLM in Engineering Applications phosphate and stripping solutions (mg/l) Amount of uranium remained in trisodium 35 30 29.86 Remained in TSP Remained in stripping solution 25 20 ... constant (cm3/mgmin) Feed- or aqueous-phase masstransfer coefficient or masstransfer ki coefficient in feed phase km Organic-phase masstransfer coefficient or masstransfer coefficient in liquid ... Stripping-phase masstransfer coefficient or masstransfer coefficient ks in stripping phase L Length of the hollow fiber (cm) LMs Liquid membranes lif Feed interfacial film thickness Stripping interfacial...
... oxygen flow rate through PVTMS membrane: – oxygen flow rate in channel 1, – overall flow rate (individual flow rates are involved with weight 0.5), – oxygen flow rate in channel 2, – oxygen flow ... nitrogen transfer) 224 MassTransferin Chemical Engineering Processes Calculation was carried out with the same main parameters which were defined in previous section Fig 16(a) represents the influence ... = 0.1 s-1; — = 0.5 s-1; — = s-1 216 MassTransferin Chemical Engineering Processes A A A sin t A AB sin t B A AB sin t AB , where A AB A A A...
... called as the mass burning rate, defined as mass transferred in unit area and time, is then determined by chemical kinetics and therefore the process is kinetically controlled In this kinetically ... Current (mA.m ) (b) Fig Effect of masstransfer area on performance of MFC 800 242 MassTransferin Chemical Engineering Processes of MFC Three different masstransfer area (3.14, 9and 16 cm2) ... 240 MassTransferin Chemical Engineering Processes In order to obtain the best oxidizer in cathode compartment, several oxidizers were analyzed Table summarized the optimum conditions obtained...
... present flow configuration, after confirming its appropriateness, being examined by varying both the freestream velocity and graphite rod diameter that can exert influences in determining velocity ... be determined by substituting the values of I, obtained from Eq (75), into Eq (66) It may be informative to note that for some weakly-burning situations, in which O2 concentrations in the reaction ... suggesting that the establishment of CO-flame can be suppressed with increasing velocity gradient Note here that in obtaining data in Figs 3(a) to 3(c), attention has been paid to controlling the...
... those in the high-temperature oxidizer-flows in Figs 5(a) and 5(b) are nearly the same as that in the room-temperature airflow in Fig 3(a) with the same massflow rate As pointed out (Makino, ... rate first increases, then decreases abruptly, and again increases, with increasing Ts, as explained in the previous Section The ignition surfacetemperature observed is about 1800 K, in accordance ... elevated with increasing air temperature, the combustion rate in the high-temperature airflow is necessarily higher than that in the room-temperature airflow Results in the room-temperature airflow with...
... transport in porous media where interphase masstransfer is important Mass and Heat Transfer During Two-Phase Flowin Porous Media - Theory and Modeling Mass and Heat Transfer During Two-Phase Flowin ... Pore-scale picture of interphase masstransfer x x Mass and Heat Transfer During Two-Phase Flowin Porous Media - Theory and Modeling Mass and Heat Transfer During Two-Phase Flowin Porous Media - ... kinetics 19 19 Mass and Heat Transfer During Two-Phase Flowin Porous Media - Theory and Modeling Mass and Heat Transfer During Two-Phase Flowin Porous Media - Theory and Modeling T l from interfacial...
... convection in porous media, Int J Heat MassTransfer 30: 143–150 Solute Transport With Chemical Reaction Single- and Multi-Phase Flowinin Porous Media Solute TransportWith Chemical Reaction inin Singleand ... boundaries in porous media, Int J Heat MassTransfer 36: 1357–1365 Udell, K S (1985) Heat transferin porous media considering phase change and capillarity – the heat pipe effect, Int J Heat MassTransfer ... 18 66 MassTransferMassTransferin Multiphase Systems and its Applications Majorana, C E (2010) An approach for modelling concrete spalling in finite strain Mathematics and Computers in Simulation,...
... slightly inclined layer Shown in Fig are the series of interferograms of the concentration field generated during surfactant dissolution from the drop in the layer inclined at an angle α = 9° As in ... impeller speed and gas flow rates, the kind of gas introduced into the vessel is changed was used The gases were air and nitrogen At the beginning of the 101 MassTransferin Multiphase Mechanically ... than in the two–phase system (Fig 8a) In coalescing system, it can be explained that solids in a small quantity during their movement in the system hit the gas bubbles, which are breaking into...
... Approach in the Modeling of Flotation Flotation TransferTransferin Gas-Liquid Contacting Modeling of and Massand Massin Gas-Liquid Contacting Systems Systems 139 139 Generally speaking, this kind ... 144 MassTransferin Multiphase Systems and its Applications MassTransferin Multiphase Systems and its Applications Local modeling of transfers in gas-liquid bubbly flows 3.1 Masstransferin ... Local Approach in the Modeling of Flotation Flotation TransferTransferin Gas-Liquid Contacting Modeling of and Massand Massin Gas-Liquid Contacting Systems Systems 141 141 In reference to...