5.3-6. Unsteady-State Conduction in a Brick Wall. A flat brick wall 1.0 ft thick is the lining on one side of a furnace. If the wall is at a uniform temperature of 100°F and one side is suddenly exposed to a gas at 1100°F, calculate the time for the furnace wall at a point 0.5 ft from the surface to reach 500°F. The rear side of the wall is insulated. The convection coefficient is 2.6 btu/h ft². °F and the physical properties of the brick are k= 0.65 btu/h ft °F and a = 0.02 ft²/h.
5.3-6. Unsteady-State Conduction in a Brick Wall. A flat brick wall 1.0 ft thick is the lining on one side of a furnace. If the wall is at a uniform temperature of 100°F and one side is suddenly exposed to a gas at 1100°F, calculate the time for the furnace wall at a point 0.5 ft from the surface to reach 500°F. The rear side of the wall is insulated. The convection coefficient is 2.6 btu/h ft². °F and the physical properties of the brick are k= 0.65 btu/h ft °F and a = 0.02 ft²/h.
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
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Transcribed Image Text:5.3-6. Unsteady-State Conduction in a Brick Wall. A flat brick wall 1.0 ft thick is the lining
on one side of a furnace. If the wall is at a uniform temperature of 100°F and one side
is suddenly exposed to a gas at 1100°F, calculate the time for the furnace wall at a
point 0.5 ft from the surface to reach 500°F. The rear side of the wall is insulated. The
convection coefficient is 2.6 btu/h ft² °F and the physical properties of the brick are
k= 0.65 btu/h ft. °F and a = 0.02 ft²/h.
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