0600-1-mt
The units of diffusivity are:
1994-1-o-mt
Diffusion coefficient in a binary gas mixture at low pressures varies with pressure as
1997-1-15-mt
Molecular diffusivity of a liquid
2003-16-mt
The diffusion coefficient, in m2/s, of acetic acid in benzene (liquid in liquid) is
2003-17-mt Component \(A\) is diffusing in a medium \(B\). The flux \(N_A\) relative to a stationary point is equal to the flux due to molecular diffusion if
2005-20-mt
The ratio of the diffusion coefficient in a gas to that in a liquid is of the order of
2006-13-mt The reaction \(2A + B \rightarrow 2C\) occurs on a catalyst surface. The reactants \(A\) and \(B\) diffuse to the catalyst surface and get converted completely to the product \(C\), which diffuses back. The steady state molar fluxes of \(A\), \(B\) and
\(C\) are related by
2011-19-mt Ammonia (component 1) is evaporating from a partially filled bottle into surrounding air (component 2). The liquid level in the bottle and the concentration of ammonia at the top of the bottle are maintained constant. \(N_i\) is the molar flux relative
to a fixed location in space and \(J_i\) is the molar flux with respect to the average molar velocity of the constituent species in the gas phase. Assume that air in the bottle is stagnant. Which ONE of the following is CORRECT ?
2015-14-mt For a binary mixture of components \(A\) and \(B\), \(N_A\) and \(N_B\) denote the total molar fluxes of components \(A\) and \(B\), respectively. \(J_A\) and \(J_B\) are the corresponding molar diffusive fluxes. Which of the following is true for equimolar
counter-diffusion in the binary mixture?
1988-15-i-mt For equimolar counter diffusion from a sphere to a surrounding stationary infinite medium, the mass flux \(N_{Ai}\) of the diffusing component \(A\) at the interface is given by \(N_{Ai} = D_A(C_{Ai} - C_{Ab})/R\) where \(D_A\) is the diffusivity, \(R\)
the radius of the sphere and \(C_{Ai}\) and \(C_{Ab}\) the molar concentrations of \(A\) at the interface and at a point far away from the sphere. Show that the Sherwood number, based on the diameter of the sphere, is equal to 2.
1988-5-a-i-mt Gas \(A\) diffuses to the surface of a catalyst where it is converted into \(B\) according to the chemical reaction \(3A\rightarrow B\). The product diffuses back. The ratio of molar flux of \(A\) to \(B\) at steady state is ––––- .
1991-6-ii-mt
The Fick’s second law of diffusion in one dimension is ––––- .
1993-22-a-mt Oxygen is diffusing in a mixture of oxygen-nitrogen at 1 std atm, 25\(^\circ \)C. Concentration of oxygen at planes 2 mm apart are 10 and 20 volume % respectively. Nitrogen is non-diffusing.
1994-19-mt In a gas mixture of hydrogen and oxygen, steady state equimolar counter diffusion is occurring at a total pressure of 100 kPa and temperature of 20\(^\circ \)C. If the partial pressures of oxygen at two planes 0.01 m apart, and perpendicular to the direction
of diffusion are 15 kPa and 5 kPa, respectively and the mass diffusion flux of oxygen in the mixture is \(1.6 \times 10^{-5}\) kmol/m\(^2\).s, calculate the molecular diffusivity (in m\(^2\)/s) for the system.
____________\(\times 10^{-5}\)
Last Modified on: 03-May-2024
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