2. It is desired to produce 10 kg.mol lime from calcinations of CaCO3 (pure) in a rotary kiln. Producer gas of composition 7.2% CO2, 1.6% O2, 16.6% CO and 74.6% N2 is combusted with 20% excess air to obtain the desired temperature in the kiln. The limestone and air are supplied at 298K, whereas producer gas is heated to 900K. Lime is discharged at 1200K and at 500K. Calculate the amount of the producer gas (1atm and 273K).

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
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2. It is desired to produce 10 kg.mol lime from calcinations of
CaCO, (pure) in a rotary kiln. Producer gas of composition 7.2%
CO,, 1.6% O, 16.6% CO and 74.6% N, is combusted with 20%
excess air to obtain the desired temperature in the kiln. The
limestone and air are supplied at 298K, whereas producer gas is
heated to 900K. Lime is discharged at 1200K and at 500K.
Calculate the amount of the producer gas (latm and 273K).
Transcribed Image Text:2. It is desired to produce 10 kg.mol lime from calcinations of CaCO, (pure) in a rotary kiln. Producer gas of composition 7.2% CO,, 1.6% O, 16.6% CO and 74.6% N, is combusted with 20% excess air to obtain the desired temperature in the kiln. The limestone and air are supplied at 298K, whereas producer gas is heated to 900K. Lime is discharged at 1200K and at 500K. Calculate the amount of the producer gas (latm and 273K).
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