Kinetic reactions Please make sure you get the same answers as written and solve all the...
Question 1: Design of isothermal reactors 30 Marks The irreversible, gas-phase reaction A+B D is to be carried out in an isotherma °C) plug-flow reactor (PFR) at 5.0 atm. The mole fractions of the feed streams are A 0 B 0.50, and inerts 0.30. The activation energy for the above reaction is 80 000 cal/mol. the pressure drop due to fluid friction in the reactor is so small that it can be ignored, perform the following tasks: 2T a s...
Hi everybody,can you help me for problem 4 in the attach . Thank for help! The elementary reversible reaction A + B 2C occurs in the liquid phase in isothermal CSTR. A stream containing equimolar amounts of A and B in a solvent enters. the reactor, and the conversion of A is measured to be 60%. The equilibrium conversion o A under the same inlet conditions is known to be 80%. The volumetric flowrate into the process is to be...
Please answer all parts 2. A total of 10000 L/h of metaxylene, C&H(CHs)2, is being isomerized to a mixture of orthoxylene, metaxylene, and paraxylene in a reactor with a volume of 1000 L. The isomerization reaction can be represented as: where A is the metaxylene being fed to the reactor, and B are the different isomers formed. The reaction is being carried out at 400°C and 20 bar. Under these conditions, 35% of the metaxylene fed to the reactor is...
Hi, can you please help me with F? I know that if the volume is the same, negative order reactions would give PFR a higher yield, however, when I tried to do it mathematically, the units won't match because of the rate constant. I don't know how to prove that PFR would give a higher yield. Can i use the same rate constant but with different units? 3. Your boss asks you to isothermally carry out a liquid-phase, irreversible reaction...
The reversible liquid reaction 2A ↔ B + C is carried out in an isothermal CSTR with no pressure drop. The feed has an A concentration of 0.1 lbmol/ft3 and T=300K. The forward reaction rate constant is 1800 ft3/lbmol-s and the concentration equilibrium constant is 0.3. a. Determine the equilibrium conversion. b. Determine the reactor volume necessary to achieve 98% of the equilibrium conversion of A if the feed is 10 lb mol/min.
The reversible gas-phase dehydrogenation of ethylbenzene is achieved in an isothermal CSTR with no pressure drop. The feed enters at a volumetric flow rate of v0 = 2000 L/hour. On a molar basis the feed consists of half ethyl benzene (A) and half inerts (I) and is well mixed before it enters the reactor. The total pressure in the reactor is 6 bar (PA0 = 3 bar, PI0 = 3 bar). The molar flow rate of A is FA0 =...
Describe your solutions in detail, because partial credit will be given based on your work. If additional information is necessary in solving the problems, DO use your engineering sense and provide reasonable assumptions and explanations. You may use your calculator if necessary. Use a language of your choice. Note: The following information may be used. Gas constant, R-8.314 J(mol K)-8.314 kPa L/(mol K)-0.082 L atm/(mol K)-6.132 lbr ft/(gmol K)=1,987 cal/(mol K). Atomic mass of N-14; Atomic mass of O= 1...
please solve it right . Example: Van de Vusse Reaction in an CSTR Van de Vusse liquid phase reaction is carried out in an isothermal CSTR according to the following stoichiometric equations: k3 where B is the desired product, and C and D are the undesired byproducts. The feed to the CSTR contains the reactant A only. The reaction rates are given by the following rate laws: 2 Additional information: k 0.8333 min k2 1.667 min, k3 0.1667 L min...
1. (40 points) Calculate the equilibrium conversion and species concentrations for each of the following reactions: (a). The liquid phase reaction A+B C with Cao = CBo = 2mol/L and K= 10. (b). The gas phase reaction A = 30 Carried out in a flow reactor with no pressure drop (P=Po) Pure A enters at a temperature, To=400K and a pressure, Po = 10 atm. At this temperature, K = 0.25. (c). The gas-phase reaction in part (b) carried out...
Design a CSTR for the elementary consecutive gas-phase reactions A - B C. Specify the reactor volume and the area of the heating coil inside the reactor for 50% conversion. a. Calculate the desired operating temperature inside the reactor. b. Calculate the volume of the reactor c. Calculate the area of the heating surface. The effluent stream should contain a ratio CB/Cc of 10. The feed is gas-phase and pure A at 400°C and 4 atm, with a molar flow...