In a roasting plant, 1000 kg per hour of molybdenum(IV) sulphide (MoS2) is roasted with 25 % excess air to obtain MoO3 calcine in a chamber-type roasting furnace. Preheated air enters the reactor at 400 K while MoS2 enters at room temperature. After the process, the waste gases leave the reactor at 1000 K, and the calcine leaves at 850 K.

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
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Chapter1: Introduction
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The major objective of a roasting process is to eliminate the Sulphur contained in the concentrate and
to provide a calcine. In a roasting plant, 1000 kg per hour of molybdenum(IV) sulphide (MoS2) is roasted
with 25 % excess air to obtain MoO3 calcine in a chamber-type roasting furnace. Preheated air enters
the reactor at 400 K while MoS2 enters at room temperature. After the process, the waste gases leave
the reactor at 1000 K, and the calcine leaves at 850 K.

d) Calculate the heat of reaction per hour (in kJ) of roasting of 1000 kg MoS2 (ref. 298 K) 
e) Calculate the heat per hour (in kJ) which is lost to the surrounding. 

Supplemental:
Mo=95.95 g/mol
S= 32.06 g/mol
O=16 g/mol
N=14 g/mol
AHMos2,298K = -276.14 kj/mol
AHMO03,298K = -745.1 kj/mol
AHsozle),298K = -296.8 kj/mol
Mean value of Cp 02 = 30.10 J/mol*K
Mean value of Cp n2 = 29.05 J/mol*K
[H°so K - H°298 K]Mo03 = 20.24 kJ/mol
Mean value of Cp so2 = 47 J/mol*K
SO2
Transcribed Image Text:Supplemental: Mo=95.95 g/mol S= 32.06 g/mol O=16 g/mol N=14 g/mol AHMos2,298K = -276.14 kj/mol AHMO03,298K = -745.1 kj/mol AHsozle),298K = -296.8 kj/mol Mean value of Cp 02 = 30.10 J/mol*K Mean value of Cp n2 = 29.05 J/mol*K [H°so K - H°298 K]Mo03 = 20.24 kJ/mol Mean value of Cp so2 = 47 J/mol*K SO2
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