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Q2: Limestone at 25 °C is fed to a continuous calcination reactor. The calcination is complete, and the products leave at 900 C. Taking 1 metrie ton (1000 kg) of limestone as a basis and elemental species [Ca(s), C(s), O (g)] at 25 C as references for enthalpy calculations. prepare and fill in an inlet-outlet enthalpy table and prove that the required heat transfer to the reactor is 2,7 X 10 kJ. Heat CaCO3 (s) Ca0 (s) + CO2 (g)

Q2: Limestone at 25 °C is fed to a continuous calcination reactor. The calcination is complete, and the products leave at 900 C. Taking 1 metrie ton (1000 kg) of limestone as a basis and elemental species [Ca(s), C(s), O (g)] at 25 C as references for enthalpy calculations. prepare and fill in an inlet-outlet enthalpy table and prove that the required heat transfer to the reactor is 2,7 X 10 kJ. Heat CaCO3 (s) Ca0 (s) + CO2 (g)

Introduction to Chemical Engineering Thermodynamics
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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Q2: Limestone at 25 °C is fed to a continuous calcination reactor. The calcination is complete, and the products leave at 900 C. Taking 1 metrie ton (1000 kg) of limestone as a basis and elemental species [Ca(s), C(s), O (g)] at 25 C as references for enthalpy calculations. prepare and fill in an inlet-outlet enthalpy table and prove that the required heat transfer to the reactor is 2,7 X 10 kJ. Heat CaCO3 (s) Ca0 (s) + CO2 (g)
Transcribed Image Text:Q2: Limestone at 25 °C is fed to a continuous calcination reactor. The calcination is complete, and the products leave at 900 C. Taking 1 metrie ton (1000 kg) of limestone as a basis and elemental species [Ca(s), C(s), O (g)] at 25 C as references for enthalpy calculations. prepare and fill in an inlet-outlet enthalpy table and prove that the required heat transfer to the reactor is 2,7 X 10 kJ. Heat CaCO3 (s) Ca0 (s) + CO2 (g)
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