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Stream 1 Mixing tee C=1 gl. V₁-10 L/min T₁-25°C Stream 3 C=3 g/L vy-30 L/min TC Stream 2 C4 g/L. V20 L/min T-55°C V=150L T-80°C 8 To reactor Heater Rework the chemical mixing scenario if at 3 P.M. the operator mistakenly increases the flow rate of stream 1 to 20 L/min while stream 2 and the heater input remain unchanged.

Stream 1 Mixing tee C=1 gl. V₁-10 L/min T₁-25°C Stream 3 C=3 g/L vy-30 L/min TC Stream 2 C4 g/L. V20 L/min T-55°C V=150L T-80°C 8 To reactor Heater Rework the chemical mixing scenario if at 3 P.M. the operator mistakenly increases the flow rate of stream 1 to 20 L/min while stream 2 and the heater input remain unchanged.

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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Solve for the temperature of the outgoing stream from tank at t=9.7min in degree Celsius.
Stream 3 C3 g/l. Vy=30 L/min Stream I Mixing tee V=10 L/min T;=25°C Ve150L C, Ta80°C Stream 2 C4 gl. Vy 20 L/min -To reactor Heater Rework the chemical mixing scenarioif at 3P.M. the oertor mistakenly increases teflow rale of stram I to 20 Lmin while steam 2 and the heaer input emain unchanged.
Transcribed Image Text:Stream 3 C3 g/l. Vy=30 L/min Stream I Mixing tee V=10 L/min T;=25°C Ve150L C, Ta80°C Stream 2 C4 gl. Vy 20 L/min -To reactor Heater Rework the chemical mixing scenarioif at 3P.M. the oertor mistakenly increases teflow rale of stram I to 20 Lmin while steam 2 and the heaer input emain unchanged.
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