QUESTION #1- HEAT EXCANGER DESIGN Design an exchanger to sub-cool methanol vapours from 95 "C to 40°c. The flowrate of methanol is 20200kg/hr. Brackish water or municipality water or river wvater or treated water can be used as the coolant with a temperature rise from 25 to 4aorc. Heat capacities of methanol and water are 2.84k/kg and 4.2 k/kgC respectively. The densities of methanol and water are 792 kg/m' and kg/m'respectively. Note: po the calculations step by step. Write formulas used in calculations in full along the calculations State all your assumptions You are free to select data from table and charts as youu need it but state reasons for the selection your choices

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
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Pls use Excel. Read question 1.and fill in the template, all necessary details must be included. Only use Excel.
A TelkomSA VOWIFI
MTNSA Go Big Go Bozza
ON 88%
36
46 ll
1 6:53
Expert Q&A
Heat Exchanger
Shell (Hot)
Tube (Cold) state formulas used, aumtions, data seleetien reasons as required
State fluide allocations
Inlet Temp. C)
Oulet Temp. ("C)
Bulk Temp. ("C)
Pres. (bar)
Phase
мос
PHYSICAL PROPERTIES OF
10 FLUIDS (choice of fuids
11 Densities the/m)
12 Heat Capasities (1/kg. "C)
s Fouling resistance (m' K.kw )
31688
3165S
14 Mass flowrate (kg/)
15 Determine Heat Duty (Js)
10 Determine Leg Mean Temperature
17 DIfference.
Overall Heat Transfer (U)
(Wim K)
Ares of heat transfer (A) (m)
AT
AT
AT
AT,
MECHANICAL DESIGN
Outside diameter (mm)
21 MECHANICAL DESIGN
22 Outside diameter (mm)
23 Inside diameter (mm)
24 Length (m)
25 Triangular, Pitch, P
26 Equivalent diameter (D.) (mm)
27 Tube Area (m)
28 Total Number tubes
29 Number passes
30 Bundle Clearance (mm)
31 Shell-Diameter/ Tube Bundle (mm)
25
21
. - 1.25d,
3,0
32
QUESTION #1- HEAT EXCANGER DESIGN
Design an exchanger to sub-cool methanol vapours from 95 *C to 40°c. The flowrate of methanol is
20200kg/hr. Brackish water or municipality water or river water or treated water can be used as the
coolant with a temperature rise from 25 to 40C. Heat capacities of methanol and water are
2.84kI/kg"C and 4.2 k/kg"C respectively. The densities of methanol and water are 792 kg/m' and 998
kg/m'respectively.
Note:
po the calculations step by step.
Write formulas used in calculations in full along the calculations
State all your assumptions.
You are free to select data from table and charts as you need it but state reasons for the
selection your choices.
Transcribed Image Text:A TelkomSA VOWIFI MTNSA Go Big Go Bozza ON 88% 36 46 ll 1 6:53 Expert Q&A Heat Exchanger Shell (Hot) Tube (Cold) state formulas used, aumtions, data seleetien reasons as required State fluide allocations Inlet Temp. C) Oulet Temp. ("C) Bulk Temp. ("C) Pres. (bar) Phase мос PHYSICAL PROPERTIES OF 10 FLUIDS (choice of fuids 11 Densities the/m) 12 Heat Capasities (1/kg. "C) s Fouling resistance (m' K.kw ) 31688 3165S 14 Mass flowrate (kg/) 15 Determine Heat Duty (Js) 10 Determine Leg Mean Temperature 17 DIfference. Overall Heat Transfer (U) (Wim K) Ares of heat transfer (A) (m) AT AT AT AT, MECHANICAL DESIGN Outside diameter (mm) 21 MECHANICAL DESIGN 22 Outside diameter (mm) 23 Inside diameter (mm) 24 Length (m) 25 Triangular, Pitch, P 26 Equivalent diameter (D.) (mm) 27 Tube Area (m) 28 Total Number tubes 29 Number passes 30 Bundle Clearance (mm) 31 Shell-Diameter/ Tube Bundle (mm) 25 21 . - 1.25d, 3,0 32 QUESTION #1- HEAT EXCANGER DESIGN Design an exchanger to sub-cool methanol vapours from 95 *C to 40°c. The flowrate of methanol is 20200kg/hr. Brackish water or municipality water or river water or treated water can be used as the coolant with a temperature rise from 25 to 40C. Heat capacities of methanol and water are 2.84kI/kg"C and 4.2 k/kg"C respectively. The densities of methanol and water are 792 kg/m' and 998 kg/m'respectively. Note: po the calculations step by step. Write formulas used in calculations in full along the calculations State all your assumptions. You are free to select data from table and charts as you need it but state reasons for the selection your choices.
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