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To enhance the effective surface, and hence the chemical reaction rate, catalytic surfaces often take the form of porous solids. One such solid may be visualized as consisting of a large number of cylindrical pores, each of diameter D and length L.
Consider conditions involving a gaseous mixture of A and B for which species A is chemically consumed at the catalytic surface. The reaction is known to be first order, and the rate at which it occurs per unit area of the surface may be expressed as
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Fundamentals of Heat and Mass Transfer
- An FCC iron-carbon alloy initially containing 0.35 wt% C is exposed to an oxygen-rich and virtually carbon-free atmosphere at 1400 K (1127°C). Under these circumstances the carbon diffuses from the alloy and reacts at the surface with the oxygen in the atmosphere; that is, the carbon concentration at the surface position is maintained essentially at 0 wt% C. (This process of carbon depletion is termed decarburization.) At what position will the carbon concentration he 0.15 wt% after a 10-h treatment? The value of D at 1400 K is 6.9 x 10m²'sarrow_forwardConsider a sheet of Iron which is maintained in an atmosphere filled with nitrogen and is permitted to achieve and steady state diffuseion. The thickness of the sheet is 6.5mm. The diffusion coefficient of nitrogen in iron is 1.9 × 10 -11 m 2 /s at 675 0 C.arrow_forwardWet air containing 4.0 mole% water vapor is passed through a column of calcium chloridepellets. The pellets adsorb 97.0% of the water and none of the other constituents of the air.The column packing was initially dry and had a mass of 3.40 kg. Following 5.0 hours ofoperation, the pellets are reweighed and found to have a mass of 3.54 kg. Calculate the molarflow rate (mol/h) of the feed gas and the mole fraction of water vapor in the product gas. Themole fraction of water in the product gas is monitored and found to have the value calculatedin part (a) for the first 10 hours of operation, but then it begins to increase.What is the most likely cause of the increase?If the process continues to run, what will the mole fraction of water in the product gaseventually be?arrow_forward
- An FCC iron–carbon alloy initially containing 0.35wt% C is exposed to an oxygen-rich and virtually carbon-free atmosphere at 1450K (1177 degree C). Underthese circumstances the carbon diffuses from the alloy and reacts at thesurface with the oxygen in the atmosphere; that is, the carbon concentration atthe surface position is maintained essentially at 0 wt% C. (This process ofcarbon depletion is termed decarburization.) At what position will thecarbon concentration be 0.15 wt% after a 15-h treatment? The value of D at1400 K is 6.9 x 10^(-11)m^2/s.arrow_forwardThe wear resistance of a steel shaft is to be improved by hardening its surface by increasing the nitrogen content within an outer surface layer as a result of nitrogen diffusion into the steel; the nitrogen is to be supplied from an external nitrogen-rich gas at an elevated and constant temperature. The initial nitrogen content of the steel is 0.0020wt%, whereas the surface concentration is to be maintained at 0.50wt%. For this application, a nitrogen content of 0.10wt% at a position 0.40 mm below the surface is desired. I. Will this process be a steady state or non-steady state process? Why? II. Would you expect nitrogen to diffuse by a vacancy mechanism or an interstitial mechanism? Why?arrow_forward4arrow_forward
- An iron-carbon alloy initially containing 0.240 wt% C is exposed to an oxygen-rich and virtually carbon-free atmosphere at 1100°C. Under these circumstances the carbon diffuses from the alloy and reacts at the surface with the oxygen in the atmosphere; that is, the carbon concentration at the surface position is maintained essentially at 0.0 wt% C. At what position will the carbon concentration be 0.180 wt% after a 7 h treatment? The value of D at 1100°C is 3.7 × 10-11 m2/s.arrow_forwardA mechanism for hardening steel is called carburization. To achieve this process, the piece of steel is exposed to an atmosphere rich in hydrocarbon such as methane (CH4). Consider a steel with a carbide concentration of 0.25wt%, which must be treated at 950˚C. If the carbon concentration at the surface is suddenly increased to 1.20wt%, how long does it take for a penetration of 0.5mm from the surface to reach a concentration of 0.80wt%? . The diffusion coefficient for carbon in iron at this temperature is 1.6 x 10-11 m2s-1. Assume that the piece of steel is semi-finite. Use the table below.arrow_forwardA membrane is to be manufactured to the following specifications. At 700°C the leak rate of hydrogen at steady state is not to exceed 103 mol cm2 hr' when the concentrations of hydrogen are maintained at Chigh = 7.7 × 1019 atoms cm³ on one side of the membrane and Clow effectively zero on the other side. Determine the minimum thickness, {, of iron foil that will meet these requirements. The diffusion coefficient of atomic hydrogen in iron, DH, at 700°C is 3.091x104 cm? s. Express your answer in units of cm.arrow_forward
- (5) The characteristic equation of gasses (PV-mRT) holds good for (a) Monoatomic gases (b) ideal gases (c) mixture of gases (d) diatomic gas (e) Non in the mentioned. (6) The processes or systems that do not involve heat are called a) Isothermal processes (b) equilibrium processes (c) thermal processes (d) (e) steady processes (f) Non in the mentioned adiabatic processes (7) Which of the following is not a property of the system? a) Heat, mentioned (b) Temperature, (c) specific volume, (d) pressure, (e) Non in the (8) During throttling process (a) Internal energy does not change, (b) pressure does not change, (c) volume change is negligible, (d) entropy does not change, (e) enthalpy does not change, (f) Non in the mentioned. (9) (a) Triple point involves equilibrium of solid, liquid and vapor phases, (b) Critical point involves equilibrium of solid and vapor phases, (c) Critical point involves equilibrium of solid and liquid phases, (d) Critical point involves equilibrium of solid,…arrow_forwardI want tge solution plsarrow_forwardProblem 1. A sheet of BCC iron 1 mm thick was exposed to a carburizing gas atmosphere on one side and a decarburizing atmosphere on the other side at 725°C. After having reached steady state, the iron was quickly cooled to room temperature. The carbon concentrations at the two surfaces of the sheet were determined to be 0.012 and 0.0075 wt%, respectively. Compute the diffusion coefficient if the diffusion flux is 1.4 × 10 -³ kg/m²-s.arrow_forward
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