Nickel carbonyl (component B) is produced by passing carbon monoxide (component A) over nickel. The following reaction takes place at the solid surface.
Ni + 4CO(g) ---> Ni(CO)4(g)
The reaction is very rapid so that the partial pressure of CO at the metal surface is essentially zero. Therefore, the rate of carbonyl formation is limited by the rate of CO diffusion to the nickel surface. The gas outside the diffusion layer (thickness = 0.695 mm) is pure CO, the temperature and pressure of the system remains constant at 50C and 1.0 atm, respectively, the area of the nickel is 0.25 m2, and DAB = 2.0 * 10-5 m2/s. Calculate the reaction rate of nickel carbonyl in kmol/s. Assume steady state behavior and ignore changes in the nickel metal.
Repeat the calculation of the reaction rate of nickel carbonyl for the case where the reaction is not diffusion limited. Assume first order kinetics (i.e., NA = k1'cxA ), with k1' = 5.63×10-4 m/s and 5.63×10-2 m/s.
On a well formatted Excel graph, plot the mole fraction profile of CO throughout the diffusion layer (i.e., xCO vs. (z/δ) for the three reaction rates.
Nickel carbonyl (component B) is produced by passing carbon monoxide (component A) over nickel. The following...
13-3 Nickel carbonyl, Ni(CO)4 is an extremely toxic liquid with a low boiling point. Nickel carbonyl results from the reaction of nickel metal with carbon monoxide. For temperatures about the boiling point of nickel carbonyl (42.2 °C), the reaction is: Ni(s) + 4 CO(g) Ni(CO)4(g) Suppose this reaction is carried, and at equilibrium, analysis shows a carbon monoxide pressure of 0.221 atm, a nickel carbonyl pressure of 0.0875 atm, and 0.4627 g of nickel. Calculate K for this reaction.
summatize the following info and break them into differeng key points. write them in yojr own words apartus 6.1 Introduction—The design of a successful hot box appa- ratus is influenced by many factors. Before beginning the design of an apparatus meeting this standard, the designer shall review the discussion on the limitations and accuracy, Section 13, discussions of the energy flows in a hot box, Annex A2, the metering box wall loss flow, Annex A3, and flanking loss, Annex...