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2015, Company PQ has planned to purchase a floating head heat exchanger with a specification in Table 3. They expand their plant in 2020 with the purchase of a larger heat exchanger from a similar supplier and also a vertical separator vessel with specification in Table 4. (Refer attachment) (a) Determine the bare module cost of the heat exchanger in year 2015 Chemical Engineering Plant Cost Index (CEPCI); 2001 = 394, 2015 = 557 (b) The Company PQ has ordered a new Floating Head Heat Exchangers but with a triple size (area) than the heat exchanger above. Based on the cost in 4(a), what would cost be for a new size heat exchanger for similar service in year of 2020 (use n=0.6). Chemical Engineering Plant Cost Index (CEPCI); 2020 = 596 (c) Determine the bare module cost of the vessel in year 2020 based on the specification below. (Refer attachment)

2015, Company PQ has planned to purchase a floating head heat exchanger with a specification in Table 3. They expand their plant in 2020 with the purchase of a larger heat exchanger from a similar supplier and also a vertical separator vessel with specification in Table 4. (Refer attachment) (a) Determine the bare module cost of the heat exchanger in year 2015 Chemical Engineering Plant Cost Index (CEPCI); 2001 = 394, 2015 = 557 (b) The Company PQ has ordered a new Floating Head Heat Exchangers but with a triple size (area) than the heat exchanger above. Based on the cost in 4(a), what would cost be for a new size heat exchanger for similar service in year of 2020 (use n=0.6). Chemical Engineering Plant Cost Index (CEPCI); 2020 = 596 (c) Determine the bare module cost of the vessel in year 2020 based on the specification below. (Refer attachment)

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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In 2015, Company PQ has planned to purchase a floating head heat exchanger with a specification in Table 3. They expand their plant in 2020 with the purchase of a larger heat exchanger from a similar supplier and also a vertical separator vessel with specification in Table 4.

(Refer attachment)

(a) Determine the bare module cost of the heat exchanger in year 2015
Chemical Engineering Plant Cost Index (CEPCI); 2001 = 394, 2015 = 557


(b) The Company PQ has ordered a new Floating Head Heat Exchangers but with a triple size (area) than the heat exchanger above. Based on the cost in 4(a), what would cost be for a new size heat exchanger for similar service in year of 2020 (use n=0.6). Chemical Engineering Plant Cost Index (CEPCI); 2020 = 596


(c) Determine the bare module cost of the vessel in year 2020 based on the specification below.

(Refer attachment)

Shell Figure 2: A schematic diagram of floating head heat exchanger Pressure: Tubes (barg) Shell (barg) Table 3: Specification for heat exchanger purchased in 2015 Design Material of construction: Number of tubes Length of tubes (m) Tube diameter (mm) Tubes Specification Carbon steel Shell Stainless-steel tubes 17 4 600 4 20
Transcribed Image Text:Shell Figure 2: A schematic diagram of floating head heat exchanger Pressure: Tubes (barg) Shell (barg) Table 3: Specification for heat exchanger purchased in 2015 Design Material of construction: Number of tubes Length of tubes (m) Tube diameter (mm) Tubes Specification Carbon steel Shell Stainless-steel tubes 17 4 600 4 20
Table 4: Specification for separator vessel Specification Carbon steel 38 °C Design Material of construction Operating temperature Pressure Orientation Height Diameter 3 barg Vertical 3.5 m 1.1 m
Transcribed Image Text:Table 4: Specification for separator vessel Specification Carbon steel 38 °C Design Material of construction Operating temperature Pressure Orientation Height Diameter 3 barg Vertical 3.5 m 1.1 m
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