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The purchased cost of a shell-and-tube heat exchanger 6632 m2 of the heating surface (floating-head and carbon-steel tubes) with a) What will be the 2015 purchased cost of a similar )was OMR 6632 in 2015 heat exchanger with 24 m2 of the heating surface if the purchased cost capacity exponent is 0.65 for surface areas ranging from 10 to 50 m2 b) If the purchased cost capacity exponent for this type of exchanger is 0.83 for surface areas ranging from 50 to 200 m2, what will be the purchased cost of a heat exchanger with 6632 m2 of heating surface in 2018 Use suitable Marshall & Swift or Chemical engineering plant cost index data values with proper referencing

The purchased cost of a shell-and-tube heat exchanger 6632 m2 of the heating surface (floating-head and carbon-steel tubes) with a) What will be the 2015 purchased cost of a similar )was OMR 6632 in 2015 heat exchanger with 24 m2 of the heating surface if the purchased cost capacity exponent is 0.65 for surface areas ranging from 10 to 50 m2 b) If the purchased cost capacity exponent for this type of exchanger is 0.83 for surface areas ranging from 50 to 200 m2, what will be the purchased cost of a heat exchanger with 6632 m2 of heating surface in 2018 Use suitable Marshall & Swift or Chemical engineering plant cost index data values with proper referencing

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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The purchased cost of a shell-and-tube heat exchanger 6632 m2 of the heating surface (floating-head and carbon-steel tubes) with a) What will be the 2015 purchased cost of a similar )was OMR 6632 in 2015 heat exchanger with 24 m2 of the heating surface if the purchased cost capacity exponent is 0.65 for surface areas ranging from 10 to 50 m2 b) If the purchased cost capacity exponent for this type of exchanger is 0.83 for surface areas ranging from 50 to 200 m2 , what will be the purchased cost of a heat exchanger with 6632 m2 of heating surface in 2018 Use suitable Marshall & Swift or Chemical engineering plant cost index data values with proper referencing
Transcribed Image Text:The purchased cost of a shell-and-tube heat exchanger 6632 m2 of the heating surface (floating-head and carbon-steel tubes) with a) What will be the 2015 purchased cost of a similar )was OMR 6632 in 2015 heat exchanger with 24 m2 of the heating surface if the purchased cost capacity exponent is 0.65 for surface areas ranging from 10 to 50 m2 b) If the purchased cost capacity exponent for this type of exchanger is 0.83 for surface areas ranging from 50 to 200 m2 , what will be the purchased cost of a heat exchanger with 6632 m2 of heating surface in 2018 Use suitable Marshall & Swift or Chemical engineering plant cost index data values with proper referencing
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