Customer Address Plant Location Service of Unit: Size Surf/unit (eff.)
PV Engineering Waterloo, ON Hot oil heater 17 / 96 213.7 ft2
Fluid allocation Fluid name Fluid quantity, Total Vapor (In/Out) Liquid Noncondensable Temperature (In/Out) Dew / Bubble point Density (Vap / Liq) Viscosity Molecular wt, Vap Molecular wt, NC Specific heat Thermal conductivity Latent heat Pressure Velocity Pressure drop, allow./calc. Fouling resist. (min) Heat exchanged Transfer rate, Service
in
Job No.: Reference No.: Proposal No.: Date: August 24, 2010 Rev. 2 Item No: E-101 Type BEM Hor Connected in 1 1 parallel Shells/unit 1 213.7 ft2 Surf/shell (eff.) PERFORMANCE OF ONE UNIT Shell Side Tube Side lb/h lb/h lb/h lb/h
10443 10443 0
572.59 F 572.59 F lb/ft3 2.625 / cp 0.0215 / 18.01
series
116667 0 10443
571.2 572.59 / 44.755 / 0.0953
0 116667
0 116667
380 578.38 / 53.323 / 0.3576
479.19 578.38 / 50.581 / 0.2262
BTU/(lb*F) 1.4586 / / 1.1674 / 0.5199 / 0.5641 BTU/(ft*h*F) 0.039 / / 0.301 / 0.079 / 0.071 BTU/lb psi 1250 1249.96 30 26.86 ft/s 2.93 6.5 psi 13.95 0.05 10 3.14 ft2*h*F/BTU 0.0005 0.001 0.0012 Ao based MTD corrected 6273921 BTU/h 140.31 F 209.93 Dirty 209.91 Clean 326.28 BTU/(h*ft2*F) CONSTRUCTION OF ONE SHELL Sketch Shell Side Tube Side Design/Vac/Test pressure FV 150 psi 1400 / / / / Design temperature 650 650 F Number passes per shell 4 1 Corrosion allowance 0.0625 0.0625 in 6 900 ANSI 1 Connections 4 In in 1 / / 300 ANSI Size/rating Out 3 900 ANSI 1 4 1 / / 300 ANSI Nominal Intermediate 900 ANSI / / 300 ANSI Tube No. 104 TksAvg 0.083 Length 96 in Pitch 1.25 in OD 1 in Tube type Plain Material Carbon Steel Tube pattern 30 Shell Carbon Steel ID 17.25 OD 19 in Shell cover Channel or bonnet Carbon Steel Channel cover Tubesheet-stationary Carbon Steel Tubesheet-floating Floating head cover Impingement protection Rods Baffle-crossing Carbon Steel Type Single segmental Cut(%d) 24.7 V Spacing: c/c 15.5 in Baffle-long Seal type Inlet 15.9375 in Supports-tube U-bend Type Bypass seal Tube-tubesheet joint Exp. 2 grv Expansion joint Carbon Steel Type Flange and flued (TEMA) RhoV2-Inlet nozzle 98 Bundle entrance 14 Bundle exit 38 lb/(ft*s2) Gaskets - Shell side Spiral-Wound Metal Fib Tube Side Spiral-Wound Metal Fib Floating head Code requirements ASME Code Sec VIII Div 1 TEMA class B - chemical service Weight/Shell 3709.1 Filled with water 4554.4 Bundle 1198.5 lb Remarks T2
S3
T1
S2
S1
Page HC Heat Transfer Solutions Inc. www.hcheattransfer.com 1-877-542-1214
1
of 5
HEAT EXCHANGER SPECIFICATION SHEET 1 2 3 4 5
Job No.: Customer Address Plant Location Service of Unit:
6 Size 7 Surf/Unit(eff) 8 9 10 11 12 13
PV Engineering Waterloo, ON Hot oil heater 17 / 213.7
located on the bottom located on the top located at rear end located at rear end
Mean Metal Wall Temperature Temperature Conditions Normal Operating Mean Wall Temperature Maximum Operating Mean Wall Temperature Startup Mean Wall Temperature Upset Mean Wall Temperature Steam Out Mean Wall Temperature Other Operating Mean Wall Temperature
Shell
Tube
573
535.89
463
480
394
240
HC Heat Transfer Solutions Inc. www.hcheattransfer.com 1-877-542-1214
Page
2
of 5
HEAT EXCHANGER SPECIFICATION SHEET 1
Job No.:
2 Customer
PV Engineering
Reference No.:
3 Address
Waterloo, ON
Proposal No.: Date:
August 24, 2010
Hot oil heater
Item No:
E-101
4 Plant Location 5 Service of Unit: 6 Size
17
7 Surf/Unit(eff)
213.7
/
96 in ft2
Type
BEM
Shells/Unit
Hor
1
Connected in Surf/Shell(eff)
1
Rev.
parallel
2 1
series
ft2
213.7
NOTES 1234-
Two (2) rows of impingement rods on a 30 deg layout are to be used for impingement protection Baffles to have a 1" V notch at the bottom The shell inlet nozzle is to be located on the side Dummy tubes (6) are to be installed in the horizontal pass partition lane.
HC Heat Transfer Solutions Inc. www.hcheattransfer.com 1-877-542-1214
Page
3
of 5
HEAT EXCHANGER SPECIFICATION SHEET 1
Job No.:
2 Customer
PV Engineering
Reference No.:
3 Address
Waterloo, ON
Proposal No.:
4 Plant Location 5 Service of Unit:
Hot oil heater
6 Size
17
7 Surf/Unit(eff)
213.7
/
96 in
Type
ft2
Shells/Unit
BEM
Hor 1
Date:
August 24, 2010
Item No:
E-101
Connected in
1
Surf/Shell(eff)
Rev.
parallel
2 1
213.7
series ser s eriies er
ft2
Tubesheet Layout
Shell inside diameter
in
17.25
Front head inside diameter
in
17.25
Outertube limit
in
16.8125
Tube number
104
Tube O.D.
in
1.
Tube pitch
in
1.25
Tube pattern
30
Tube passes
4
Tie rod number
-1
Tie rod diameter
in
0.376
Sealing strips (pairs)
0
Baffle type
Single segmental
Impingement protection
Rods
Tube length
in
96.
Shell Side Inlet Nozzle Inside Diameter
in
5.761
Shell Side Outlet Nozzle Inside Diameter
in
3.068
Shell Side Outlet Nozzle Inside Diameter
in
2.067
Cu stome r: H&C Heat Tra nsfe r So l utions Ad dres s: Sarni a , ON
Aspen Shell & Tube
Se rvice o f Un it: Ite m No.:E-10 1
Tube Layout
1.0 0
24
28
Design Codes ASME Code Sec VIII Div 1 TE MA B - chemical service
Drawing Number CustomerSpecifications 1.2 5
24
28
HC Heat Transfer Solutions Inc. www.hcheattransfer.com 1-877-542-1214
Revision
Date 24/08/2010
Dwg.
Page
App.
4
of 5
HEAT EXCHANGER SPECIFICATION SHEET 1
Job No.:
2 Customer
PV Engineering
Reference No.:
3 Address
Waterloo, ON
Proposal No.:
Hot oil heater
Item No:
4 Plant Location
Date:
5 Service of Unit: 6 Size
17
7 Surf/Unit(eff)
213.7
/
96 in
Type
ft2
Shells/Unit
BEM
Hor
August 24, 2010 Rev.
Connected in
1
2
E-101 1
parallel
Surf/Shell(eff)
1
213.7
series ser s eries es
ft2
Setting Plan V iews on arrow A
A
3.25
131.125 Overall
T2
11.125
7.125
6.5
81.0
T2
S3
T1
S2
T1
3.25
S1 S3
S2
16
7.125 Pul li ng Length
S1
19.1875
57.625
79 2.0
2.0
4.0
4.0
2 Bolts Fi xed
Ref S1 S2 S3 T1 T2
OD 6.625" 3.5" 2.375" 4.5" 4.5"
W all 0. 432" 0. 216" 0. 154" 0. 237" 0. 237"
Nozzle Data Standard 900 ANSI W eld 900 ANSI W eld 900 ANSI W eld 300 ANSI W eld 300 ANSI W eld
Notes neck ck neck eck neck ck neck neck
Design Data Design Pressure Design T emperature F ull Vacuum Corrosion Allowance T est P ressure Number of Passes Radiography PWHT Internal V olum e
Units psi F
2 Bolts Sliding
Shell 1399.99 650.
Channel 150. 650.
C u sto me r : H&C H ea t Tr a n sfe r So lutio n s
Aspen Shell & Tube Exchang er
Ad dr e s s : Sar n ia , O N Se r vic e o f Un it: Ite m N o .:E- 10 1
in psi
ft³
0. 0625
0.0625
1
4
12. 5125
4.4291
D a te: Au g 20 1 0
R ev N o .: 1
Setting Plan
J ob N o .:
BEM 17 - 96
Design Codes ASME Section VII I Div. 1 T EMA B
Drawing Number Customer Specificat ions
Empty 3709 lb
W eight Summary F looded 4554 lb
Bundle 1198 lb
HC Heat Transfer Solutions Inc. www.hcheattransfer.com 1-877-542-1214
