For the setup in Problem 22.25, do the following:

1. Reconfigure the utility flow to be countercurrent with the process gas and determine the conversion of IPA.

2. Sketch the temperature concentration profiles in a single reactor tube.

Problem 22.25

Consider the dehydration of isopropyl alcohol (IPA) to yield acetone and hydrogen:

This reaction is endothermic, with a heat of reaction of 57.2 kJ/mol. The reaction is kinetically controlled and occurs in the vapor phase over a catalyst. The reaction kinetics for this reaction are first order with respect to the concentration of alcohol and can be estimated from the following equation:

where E_a = 72.38 MJ/kmol, k_o = 1.931×10⁵ m³ (gas)/m³ (reactor)/s, and c_IPA has units of kmol/m³ (gas).

The feed to the reactor is 87 wt% IPA in water at 240°C and 2 bar. Spherical catalyst particles (5 mm in diameter) are placed in 50 mm ID tubes of length 6 m. The heat transfer coefficient on the tube side of the reactor is limiting. A heat transfer medium (HTM) is available as part of a heating loop that supplies the HTM to the reactor shell at 400°C.

Properties of the heat transfer fluid are

Properties of the process gas are

Properties of the catalyst are

1. Determine the conversion of alcohol to acetone assuming that the HTM flows cocurrently with the process gas. Assume that the HTM flows at a rate of 200,000 kg/h, the inlet flowrate to the reactor is 8,000 kg/h of IPA and water, and the reactor has a total of 1600 tubes arranged on a square pitch with the tube centers 75 mm apart.

2. Sketch the temperature concentration profiles in a single reactor tube.

Transcribed Image Text:

(CH3),CHOH*(CH3),CO+H2 IPA acetone