A hydrocarbon liquid enters a simple flow system shown at an average velocity of 1.282 m/s, where A1= 4.33 × 10^−3 m^1and ρ1= 902 kg/m3. The liquid is heated in the process and the exit density is 875 kg/m3. The cross-sectional area at point 2 is 5.26 × 10^−3 m2. The process is steady state. a. Calculate the mass flow rate ??̇ at the entrance and exit. b. Calculate the average velocity υ in 2 and the mass velocity G in 1
A hydrocarbon liquid enters a simple flow system shown at an average velocity of 1.282 m/s, where A1= 4.33 × 10^−3 m^1and ρ1= 902 kg/m3. The liquid is heated in the process and the exit density is 875 kg/m3. The cross-sectional area at point 2 is 5.26 × 10^−3 m2. The process is steady state. a. Calculate the mass flow rate ??̇ at the entrance and exit. b. Calculate the average velocity υ in 2 and the mass velocity G in 1
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 hydrocarbon liquid enters a simple flow system shown at an average velocity of 1.282 m/s, where A1= 4.33 × 10^−3 m^1and ρ1= 902 kg/m3. The liquid is heated in the process and the exit density is 875 kg/m3. The cross-sectional area at point 2 is 5.26 × 10^−3 m2. The process is steady state. a. Calculate the mass flow rate ??̇ at the entrance and exit. b. Calculate the average velocity υ in 2 and the mass velocity G in 1.
Transcribed Image Text:A1
A2
V2
P2
V1
process
P1
FIGURE 2.6-1. Mass balance on flow system.
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