Ugi ng Rot water (feno rate = 8 - 28 m³ /h ,mlet tenenature = 221°F, butlet temperature I5 , 39 °F |55 , 39 °F), CgHy O ou ethanol i being he ated from 98. 6 °F ( flow rode = 12-6 though a 1-2 shell and fube pass heat exehanger. auer age heat capacity CoHu0 = 1.63 B tu /ib of heat traws fer coef ficient %3D overall Uo = 363, 99 8tu h fte %3D Solve for : area reqpuired outlet tunperature for heat exchang er if heat trans fer rete of 5.8 x1o5 ethanol = Watts %3D ) corecti on factor, mean temperature diffe rence tmperatue Not yxehanger, Log mean difference of this
Ugi ng Rot water (feno rate = 8 - 28 m³ /h ,mlet tenenature = 221°F, butlet temperature I5 , 39 °F |55 , 39 °F), CgHy O ou ethanol i being he ated from 98. 6 °F ( flow rode = 12-6 though a 1-2 shell and fube pass heat exehanger. auer age heat capacity CoHu0 = 1.63 B tu /ib of heat traws fer coef ficient %3D overall Uo = 363, 99 8tu h fte %3D Solve for : area reqpuired outlet tunperature for heat exchang er if heat trans fer rete of 5.8 x1o5 ethanol = Watts %3D ) corecti on factor, mean temperature diffe rence tmperatue Not yxehanger, Log mean difference of this
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
Related questions
Question
![Pnoblem # 20.
Ugi ng hot water C reow rate = 8.28 m³ Ih , mlet tenpenature=
155,39 °F), Ca Hy O or
221°F, outhet temperature
ethanol is
being he ated rom
98. 6 °F C rade = 12-6
m3 /h
98. 6 °F ( Hlow rade = 12-6
through a
shell and fube
1-2
pass
heat exchanger.
heat ņ CoHG O = 1.63 B tu llb oF
capacity
%3D
heat traws fer coef ficie nt
Uo = 363, 99 8tu h ft"F
over all
%3D
Solve for
for heat exchanger
area recquired
outlet temperature if heau trans fer raste of
ethanol = 5.810
Watts
%3D
C) , ,
log mean tmperatue
this heat exehanger.
me an temperature diffe rence
difference of
corecti on factor](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2Fcb3bfa1d-7903-41f6-9afd-0dc552f717b6%2Fa8c9f6ff-f755-4f67-8b65-f255b7f9ea15%2Fg29mzi_processed.jpeg&w=3840&q=75)
Transcribed Image Text:Pnoblem # 20.
Ugi ng hot water C reow rate = 8.28 m³ Ih , mlet tenpenature=
155,39 °F), Ca Hy O or
221°F, outhet temperature
ethanol is
being he ated rom
98. 6 °F C rade = 12-6
m3 /h
98. 6 °F ( Hlow rade = 12-6
through a
shell and fube
1-2
pass
heat exchanger.
heat ņ CoHG O = 1.63 B tu llb oF
capacity
%3D
heat traws fer coef ficie nt
Uo = 363, 99 8tu h ft"F
over all
%3D
Solve for
for heat exchanger
area recquired
outlet temperature if heau trans fer raste of
ethanol = 5.810
Watts
%3D
C) , ,
log mean tmperatue
this heat exehanger.
me an temperature diffe rence
difference of
corecti on factor
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