Fluid oolig Shell & Tube Series WTE OOED opper & Steel ostructio Features Youg Touchstoe Iterchage (Thermal) optioal No-Ferrous ostructio ompetitively Priced 1/4 or 3/8 Tubes Stadard Water to Water pplicatios Sea Water pplicatios Optioal 90/10 opper Nickel oolig Tubes ad roze Ed oets for Sea Water Service, SE O-ig, SE Flage, or SPP Shell Side oectios vailable Ed oets emovable for Servicig Moutig Feet Icluded (May be otated i 90 Icremets) atigs Maximum Shell Pressure 250 psi Maximum Tube Side Pressure 150 psi Maximum Temperature 350 F Materials Tubes opper Hubs & Tubesheets Steel or rass Shell Steel or rass aff les rass Ed oets ast Iro Moutig rackets Steel askets Nitrile ubber/ellulose Fiber Nameplate lumium Foil How to Order Model Series S SF S M F FM Model Size Selected aff le Spacig - 1.125-2.25-4.5 D - 9.0 Tube Diameter ode 4-1/4 6-3/8 Tubeside Passes 0 - Oe Pass T - Two Pass F - Four Pass Shell Material lak - Steel - rass oolig Tube Material lak - opper N - uni Ed oet Material lak - ast Iro - roze DD FO SEIES MODES ONY: -N--Z is to be used for all seawater/dirty water applicatios. Zic odes lak - Noe Z - Zic Steel Hub S = Shell Side, Tube Side SF = SE Flage (with UN threads) Shell Side coectios; Tube Side coectios rass Hub = Shell Side coectios; Tube Side coectios S = SE O-ig Shell Side coectios; Tube Side coectios M = SPP Shell Side coectios; SPP Tube Side coectios F = SE Flage (with UN threads) Shell Side coectios; Tube Side coectios FM = SE Flage (with Metric threads) Shell Side coectios; SPP Tube Side coectios SE flages available o some models. osult factory for details.
Dimesios Oe Pass M Z (4 places) HH N P E J P H (2 each ed) D Flage Size HH Z - F Z - FM 1 1.03 2.06 3/8-16 UN M-10 1.41 2.75 1/2-13 UN M-12 2 1.69 3.06 3 2.44 4.19 5/8-11 UN M-16 F OOED MODE -401-402 -701-702 -703-1002 -1003-1004 -1202-1203 -1204-1205 -1206-1207 -1208-1602 -1603-1604 -1605-1606 -1607-1608 -1609-1610 2.125 3.656 5.125 6.125 8.00 7.62 16.62 7.00 16.00 25.00 15 24 33 14.62 23 32 41 50 59 68 13.60 22.60 31.60 40.60 49.60 58.60 67.60 76.60 85.60 3 6.25 7 8.81 12.13 /SPP SE O-IN SE FNE /F 8.46 10 15.61 D E F H J 11.01 20.01 12.01 21.01 30.01 21.71 30.71 39.71 2 30 39.25 48.25 57 66 75.25 22 31 40 49 58 67 76 85 94 1.94 3.62 4.75 6 2.62 5.25 6.75 7 8.62.88 3.41 Dia..44 x.88 (6) /SPP FNE * SE O-IN #8, 3/4-16 UNF-2 #16, 1 5 /16-12 UNF-2 #24, 1 7 /8-12 UN-2 #32, 2 1 /2-12 UN-2 1.72 2.69 3.06 3.44 4.39 M N P 11.24 20.24 13.64 22.64 31.64 23.60 32.60 41.60 24 33.25 42.12 51.12 60.25 69.25 78.12 26.62 35.62 44.62 53.62 62.62 71.62 80.62 89.62 98.62 1.81 3.24 4.05 4.88 6.52 (4) (4) -401 ad -402 SE Flage ot available. NOTE: We reserve the right to make reasoable desig chages without otice. osult factory. ll dimesios are iches. WTE
Dimesios Two Pass M Z (4 places) HH N E WTE OOED H (2 each ed) J D Flage Size HH Z - F Z - FM 1 1.03 2.06 3/8-16 UN M-10 1.41 2.75 1/2-13 UN M-12 2 1.69 3.06 3 2.44 4.19 5/8-11 UN M-16 F MODE -701-702 -703-1002 -1003-1004 -1202-1203 -1204-1205 -1206-1207 -1208-1602 -1603-1604 -1605-1606 -1607-1608 -1609-1610 3.656 5.125 6.125 8.00 7.00 16.00 25.00 15 24 33 14.62 23 32 41 50 59 68 13.60 22.60 31.60 40.60 49.60 58.60 67.60 76.60 85.60 /SPP SE SE O-IN FNE 6.25 7 8.81 12.13 /F 8.46 10 15.61 D E F H J 12.01 21.01 30.01 21.71 30.71 39.71 2 30 39.25 48.25 57 66 75.25 22 31 40 49 58 67 76 85 94 3.62 4.75 6 NOTE: We reserve the right to make reasoable desig chages without otice. osult factory. ll dimesios are iches. 5.25 6.75 7 8.62 3.44 x.88 (6) /SPP FNE SE O-IN #16, 1 5 /16-12 UNF-2 #24, 1 7 /8-12 UN-2 #32, 2 1 /2-12 UN-2 2.69 3.06 3.44 4.39 M N P 13.28 22.28 31.28 23.29 32.29 41.29 23.94 32.81 41.69 50.69 59.81 68.81 77.69 25.10 34.10 43.10 52.10 61.10 70.10 79.10 88.10 97.10 3.30 3.80 4.56 6.08.88 1.19 1.44 1.88
Dimesios Four Pass M Z (4 places) HH N S S E P J D H (2 each ed) F Flage Size HH Z - F Z - FM 1 1.03 2.06 3/8-16 UN M-10 1.41 2.75 1/2-13 UN M-12 2 1.69 3.06 3 2.44 4.19 5/8-11 UN M-16 OOED MODE -701-702 -703-1002 -1003-1004 -1202-1203 -1204-1205 -1206-1207 -1208-1602 -1603-1604 -1605-1606 -1607-1608 -1609-1610 3.656 5.125 6.125 8.00 7.00 16.00 25.00 15 24 33 14.62 23 32 41 50 59 68 13.60 22.60 31.60 40.60 49.60 58.60 67.60 76.60 85.60 /SPP SE O-IN 6.25 7 8.81 12.13 SE FNE /F 8.46 10 15.61 D E F H J 12.01 21.01 30.01 21.71 30.71 39.71 2 30 39.25 48.25 57 66 75.25 22 31 40 49 58 67 76 85 94 3.62 4.75 6 5.25 6.75 7 8.62 3.44 x.88 (6) /SPP FNE SE O-IN #16, 1 5 /16-12 UNF-2 #24, 1 7 /8-12 UN-2 #32, 2 1 /2-12 UN-2 2.69 3.06 3.44 4.39 M N P 13.57 22.57 31.57 23.57 32.57 41.57 24.44 33.31 42.19 51.19 60.31 69.31 78.19 26.72 35.72 44.72 53.72 62.72 71.72 80.72 89.72 98.72 3.32 4.12 4.90 6.48 (3) (1) (3).75.62.75 1.06 1 S.88 1.34 1.40 1.88 NOTE: We reserve the right to make reasoable desig chages without otice. osult factory. ll dimesios are iches. WTE
Performace urves WTE OOED Horsepower emoved i ooler 600 500 400 300 200 100 80 60 50 40 30 20 10 8 6 5 4 3 2 1 1 2 9 20 18 23 10 6 7 3 13 25 14 16 21 29 27 5 4 8 17 11 15 12 31 22 19 OI P 24 = 5 PSI = 10 PSI = 20 PSI 1 2 3 4 5 6 8 10 20 30 40 50 60 80 100 150 200 PM Oil Through ooler 30 28 26 Ship Wt. Model (lbs) *1. -401-4-0 7 *2. -402-4-0 10 *3. -701-4-T 23 4. -701-6-F 23 5. -701-6-T 23 *6. -702-4-T 28 7. -702-4-F 28 8. -702-6-T 28 *9. -703-4-T 35 10. -703-4-F 35 11. -1002-4-T 49 12. -1002-6-T 49 13. -1003-4-F 65 14. -1003-4-T 65 15. -1003-6-T 65 16. -1004-4-T 72 17. -1004-6-T 72 *18. -1202-4-F 72 19. -1202-4-F 72 *20. -1204-4-F 110 21. -1204-4-F 110 22. -1206-D4-F 160 *23. -1602-4-F 145 24. -1602-4-F 145 25. -1604-4-F 195 26. -1604-D4-F 195 27. -1606-4-F 259 28. -1606-D4-F 259 29. -1608-4-F 310 30. -1608-D4-F 310 31. -1610-D4-F 400 Shippig weights are approximate Pipig Hook-up Maximum Flow ates Example Model No. - 1003-4 - F OUT Oe Pass HOT FUID IN Uit Shell Side (PM) aff le Spacig Tube Side (PM) Size D O T F 400 9.6 25 700 17 29 29 61 31 15 1000 24 48 69 69 146 73 37 1200 29 57 115 115 224 112 56 1600 37 74 149 253 363 181 91 IN Two ad Four Pass HOT FUID (MY E EVESED) OUT OOIN WTE OOIN WTE autio: Icorrect istallatio ca cause this product to fail prematurely, causig the shell side ad tube side fluids to itermix. Specific applicatios may have differet pipig arragemets. otact factory for assistace.
Selectio Procedure Performace urves are based o 100SSU oil leavig the cooler 40 F higher tha the water temperature used for coolig. This is also referred to as a 40 F approach temperature. urves are based o a 2:1 oil to water flow ratio. *urves are 1:1. Step 1 Determie the Heat oad. This will vary with differet systems, but typically coolers are sized to remove 25 to 50% of the iput ameplate horsepower. (Example: 100 HP Power Uit x.33 = 33 HP Heat load.) If TU/Hr. is kow: HP = TU/Hr 2545 Step 2 Determie pproach Temperature. Desired oil leavig cooler F Water Ilet temp. F = ctual pproach (Max. reservoir temp.) Step 3 Step 4 Step 5 Determie urve Horsepower Heat oad. Eter the iformatio from above: Horsepower heat load x 40 x Viscosity urve ctual orrectio = Horsepower pproach Eter curves at oil flow through cooler ad curve horsepower. y curve above the itersectig poit will work. Determie Oil Pressure Drop from urves: j = 5 PSI; M = 10 PSI; l = 20 PSI. Multiply pressure drop from curve by correctio factor foud o oil viscosity correctio curve. Oil Temperature Oil coolers ca be selected usig eterig or leavig oil temperatures. Typical operatig temperature rages are: Hydraulic Oil 110 F - 130 F Hydrostatic Drive Oil 130 F - 180 F, earig ube Oil 120 F - 160 F ube Oil ircuits 110 F - 130 F. VISOSITY OETION 5 4 3 2.5 2 1.5 1.8.7.6.5 50 60 70 80 100 150 200 250 300 400 500 OI VISOSITY - SSU OOED Desired eservoir Temperature etur ie oolig: Desired temperature is the oil temperature leavig the cooler. This will be the same temperature that will be foud i the reservoir. Off-ie ecirculatio oolig oop: Desired temperature is the oil temperature eterig the cooler. I this case, the oil temperature chage must be determied so that the actual oil leavig temperature ca be foud. alculate the oil temperature chage (oil st) with this formula: Oil st = (TU s/hr.) / (PM Oil Flow x 210). To calculate the oil leavig temperature from the cooler, use this formula: Oil eavig Temp. = Oil Eterig Temp Oil st. This formula may also be used i ay applicatio where the oly temperature available is the eterig oil temperature. Oil Pressure Drop: Most systems ca tolerate a pressure drop through the heat exchager of 20 to 30 PSI. Excessive pressure drop should be avoided. are should be take to limit pressure drop to 5 PSI or less for case drai applicatios where high back pressure may damage the pump shaft seals. WTE