#3The first step in the reaction sequence for the production of nitricacid via the oxidation of ammonia is:4NH3 + 502 2 4NO + 6H2O75% conversion is achieved with an equimolar mixture of ammonia andoxygen fed at the rate of 100 mol/h. Determine the outlet compositions. (Hint:determine the limiting reactant).

A limiting reagent is a reactant that gets used up completely when the reaction is completed. The…

Answered: #3 acid via the oxidation of ammonia…

Introduction to Chemical Engineering Thermodynamics

8th Edition

ISBN:9781259696527

Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart

Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart

Chapter1: Introduction

Section: Chapter Questions

Problem 1.1P

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One of the ways that benzene is produced on a large scale is the hydrodealkylation of toluene. C,H,CH; + H, C,H, + CH4 A stream of toluene is mixed with a recycle stream and enters a reactor along with a stream of pure hydrogen. The reaction products at 550 °C enter a condenser, where they are cooled to 41.0 °C. A vapor stream containing Y5CH, = 0.600 mol CH,/mol leaves the process, and a liquid stream containing x66 = 0.810 mol benzene/mol and x6 = 0.190 mol toluene/mol enters a distillation column. The distillate of the column leaves the process at n7 = 668.0 mol/h and contains y7h = 0.9000 mol benzene/mol and y7 = 0.1000 mol toluene/mol. The bottoms of the column contains X8b = 0.250 mol benzene/mol and xgt = 0.750 mol toluene/mol and is recycled back to the fresh feed. Hydrogen is fed into the process at ni = 1183 mol H,/h. This process is carried out at 760 mmHg. A n, mol/h mol H/mol YSH2 YSCH, mol CH_/mol Ysh mol b/mol Ys mol t/mol n̟ mol/h n, mol/h Condenser Улн, тol H/mol Усн,…
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1. In a process for the manufacture of chlorine by direct oxidation of HCI with air over a catalyst to form Cl₂ and H₂O (only), the exit product is composed of HCI (4.4%), Cl₂ (19.8%), H₂O (19.8%), O₂ (4.0%), and N₂ (52.0%). The chemical reaction involved is as follow: 4HC1+02 → 2Cl2 + 2H₂0 Find a) limiting reactant and excess reactant, b) percent excess reactant, c) degree of completion of the reaction, d) extent of reaction
2. 100 moles/h of methane is burned with 100% excess air. The percent conversion of methane is 70%. Of the methane burned, 32% is reacted in partial combustion (reaction 2) and the balance reacts in complete combustion (reaction 1). The reactions are shown below: (1) CH4 + 202 3 CH4 + ; со, + 2H,0 (2) → C0 + 2H,0 a. Draw and label the flow chart for this process. Use variable notation to label the molar flow rate of each components in the streams. b. Calculate the inlet molar flowrate of air. c. Determine the extents of each reaction, §, & }2. d. Calculate the total molar flowrate in moles/h and mole fraction composition of the stack gas on a wet basis (this includes water). e. Calculate the total molar flowrate in moles/h and mole fraction composition of the stack gas on a dry basis (this does not include the water).
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Examine the reaction equation below. "Heat" being present on the reactant side of an equation indicates what? "Heat" + 2NH3 N2 + 3H2
W.W. Heckert et E. Mack studied the decomposition of ethylene oxide in gas phase at 25°C (C₂H4O → CH4 + CO), and found that it is a first-order reaction in the reactant. Determine the reaction rate constant using the date given below, for a reaction that begins with a pure reactant: time (min) Ptot (torr) 0 115.30 6 122.91 7 124.51 8 126.18 10 129.10

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