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Two streams are mixed in an adiabatic mixer, as shown in the figure. It is known that: • Stream 1 is saturated liquid/saturated vapour mixture at 1 bar with flow rate 0.82 kg/s and quality 0.88 • Stream 2 is superheated vapour at 1 bar and 480°C and flow rate 1.41 kg/s • Stream 3 (the product stream) will be at 1 bar. Neglect kinetic and potential energy changes and calculate the temperature of the product stream 3, in °C. 1 (2) Mixer (3

Two streams are mixed in an adiabatic mixer, as shown in the figure. It is known that: • Stream 1 is saturated liquid/saturated vapour mixture at 1 bar with flow rate 0.82 kg/s and quality 0.88 • Stream 2 is superheated vapour at 1 bar and 480°C and flow rate 1.41 kg/s • Stream 3 (the product stream) will be at 1 bar. Neglect kinetic and potential energy changes and calculate the temperature of the product stream 3, in °C. 1 (2) Mixer (3

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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Two streams are mixed in an adiabatic mixer, as shown in the figure. It is known that: • Stream 1 is saturated liquid/saturated vapour mixture at 1 bar with flow rate 0.82 kg/s and quality 0.88 • Stream 2 is superheated vapour at 1 bar and 480°C and flow rate 1.41 kg/s • Stream 3 (the product stream) will be at 1 bar. Neglect kinetic and potential energy changes and calculate the temperature of the product stream 3, in °C. (1 (2) Mixer 3
Transcribed Image Text:Two streams are mixed in an adiabatic mixer, as shown in the figure. It is known that: • Stream 1 is saturated liquid/saturated vapour mixture at 1 bar with flow rate 0.82 kg/s and quality 0.88 • Stream 2 is superheated vapour at 1 bar and 480°C and flow rate 1.41 kg/s • Stream 3 (the product stream) will be at 1 bar. Neglect kinetic and potential energy changes and calculate the temperature of the product stream 3, in °C. (1 (2) Mixer 3
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