A 3.00 x 10^4 -liter storage tank was taken out of service to repair and reattach a feed line damaged in a collision with a tanker. The tank was drained and then opened several days later for a welder to enter and perform the required work. No one realized, however that a large volume of liquid nonane (C9H20) remained in a collection sump at the bottom of the tank after the draining had been completed. Nonane has a lower explosion limit of 0.80 mole% and an upper explosion limit of 2.90 mole%* (i.e., nonane-air mixtures at 1 atm can explode when exposed to a spark or flame if the nonane mole fraction is between the two given values). A. Use the Antoine equation (6.1-4) to estimate the temperature at which the system would have to equilibrate in order for the gas in the tank to be at the lower explosion limit (P=1 atm). B. How many liters of liquid nonane would be required to evaporate in order to meet the lower explosion limit? C. Use the Antoine equation (6.1-4) to estimate the temperature at which the system would have to equilibrate in order for the nonane in the tank gas to reach a mole fraction of 0.012?
A 3.00 x 10^4 -liter storage tank was taken out of service to repair and reattach a feed line damaged in a collision with a tanker. The tank was drained and then opened several days later for a welder to enter and perform the required work. No one realized, however that a large volume of liquid nonane (C9H20) remained in a collection sump at the bottom of the tank after the draining had been completed. Nonane has a lower explosion limit of 0.80 mole% and an upper explosion limit of 2.90 mole%* (i.e., nonane-air mixtures at 1 atm can explode when exposed to a spark or flame if the nonane mole fraction is between the two given values). A. Use the Antoine equation (6.1-4) to estimate the temperature at which the system would have to equilibrate in order for the gas in the tank to be at the lower explosion limit (P=1 atm). B. How many liters of liquid nonane would be required to evaporate in order to meet the lower explosion limit? C. Use the Antoine equation (6.1-4) to estimate the temperature at which the system would have to equilibrate in order for the nonane in the tank gas to reach a mole fraction of 0.012?
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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A 3.00 x 10^4 -liter storage tank was taken out of service to repair and reattach a feed line damaged in a collision with a tanker.
The tank was drained and then opened several days later for a welder to enter and perform the required work.
No one realized, however that a large volume of liquid nonane (C9H20) remained in a collection sump at the bottom of the tank after the draining had been completed.
Nonane has a lower explosion limit of 0.80 mole% and an upper explosion limit of 2.90 mole%* (i.e., nonane-air mixtures at 1 atm can explode when exposed to a spark or flame if the nonane mole fraction is between the two given values).
A. Use the Antoine equation (6.1-4) to estimate the temperature at which the system would have to equilibrate in order for the gas in the tank to be at the lower explosion limit (P=1 atm).
B. How many liters of liquid nonane would be required to evaporate in order to meet the lower explosion limit?
C. Use the Antoine equation (6.1-4) to estimate the temperature at which the system would have to equilibrate in order for the nonane in the tank gas to reach a mole fraction of 0.012?
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