2. a. Satufated steam at 100 kPa is discharged from a turbine at a rate of 1150 kg/h. Superheated steam at 300 °C and 100 kPa is needed as a feed to a heat exchanger. To produce it, the turbine discharge stream is mixed with superheated steam available from a second source at 400 °C and 100 kPa. The mixing unit operates adiabatically. Calculate i. the quantity of superheated steam at 300 °C produced. ii. the required volumetric flowrate of the 400 °C steam.
2. a. Satufated steam at 100 kPa is discharged from a turbine at a rate of 1150 kg/h. Superheated steam at 300 °C and 100 kPa is needed as a feed to a heat exchanger. To produce it, the turbine discharge stream is mixed with superheated steam available from a second source at 400 °C and 100 kPa. The mixing unit operates adiabatically. Calculate i. the quantity of superheated steam at 300 °C produced. ii. the required volumetric flowrate of the 400 °C steam.
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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Transcribed Image Text:2.
a. Satufated steam at 100 kPa is discharged from a turbine at a rate of 1150 kg/h.
Superheated steam at 300 °C and 100 kPa is needed as a feed to a heat exchanger. To
produce it, the turbine discharge stream is mixed with superheated steam available
from a second source at 400 °C and 100 kPa. The mixing unit operates adiabatically.
Calculate
i. the quantity of superheated steam at 300 °C produced.
ii. the required volumetric flowrate of the 400 °C steam.
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