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.
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
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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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.
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