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Calculation of A Kerosene-Crude Oil Exchanger

This document summarizes the calculation of a heat exchanger to transfer heat between a 42° API kerosene stream and a 34° API mid-continent crude oil stream. It provides key parameters like flow rates, temperatures, exchanger geometry, and heat transfer calculations to determine the required heat transfer area and heat transfer rate between the two streams.
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0% found this document useful (0 votes)
130 views2 pages

Calculation of A Kerosene-Crude Oil Exchanger

This document summarizes the calculation of a heat exchanger to transfer heat between a 42° API kerosene stream and a 34° API mid-continent crude oil stream. It provides key parameters like flow rates, temperatures, exchanger geometry, and heat transfer calculations to determine the required heat transfer area and heat transfer rate between the two streams.
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
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Download as XLSX, PDF, TXT or read online on Scribd
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Calculation of a Kerosene-Crude Oil Exchanger

Wh = 43800 lb/hr (42o API Kerosene) T1 = 390 oF T2 =


Wc = 146787.5 lb/hr (34o API Mid-continent) t2 = 170 oF t1 =

Dirt factor : Rd = 0.003


Permissible pressure drop : ΔP = 10 psi

Available for this service : HE 1-4


Shell side : Tube side :
ID = 21.25 in Nt = 158
B= 5 in OD = 1 in
passes = 1 BWG = 13
Pt = 1.25 in
passes = 4
L= 16 f
LMTD = 152.1959

Mencari FT : (Fig 18) Mencari luas perpindahan panas tersedia :


R= 2.714286 Table.10
S= 0.241379 available heat transfer surface : 0.2618 f2/lin f
Ft = 0.92 Ad = 661.8304 f2
Ud = 54.33073 BTU/(hr.f2.oF)
ΔT = 140.0203
200 oF Q= 5034810 CP = 0.605
100 oF Q= 5034810 CP = 0.49

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