Fluid Cooling Shell & Tube B Series
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1 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 D 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.
2 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 /8-16 UN M /2-13 UN M /8-11 UN M-16 F OOED MODE /SPP SE O-IN SE FNE /F D E F H J 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 M N P (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
3 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 /8-16 UN M /2-13 UN M /8-11 UN M-16 F MODE /SPP SE SE O-IN FNE /F D E F H J NOTE: We reserve the right to make reasoable desig chages without otice. osult factory. ll dimesios are iches 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 M N P
4 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 /8-16 UN M /2-13 UN M /8-11 UN M-16 OOED MODE /SPP SE O-IN SE FNE /F D E F H J 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 M N P (3) (1) (3) S NOTE: We reserve the right to make reasoable desig chages without otice. osult factory. ll dimesios are iches. WTE
5 Performace urves WTE OOED Horsepower emoved i ooler OI P 24 = 5 PSI = 10 PSI = 20 PSI PM Oil Through ooler Ship Wt. Model (lbs) * * * T F T 23 * T F T 28 * T F T T F T T T T 72 * F F 72 * F F D4-F 160 * F F F D4-F F D4-F F D4-F D4-F 400 Shippig weights are approximate Pipig Hook-up Maximum Flow ates Example Model No F OUT Oe Pass HOT FUID IN Uit Shell Side (PM) aff le Spacig Tube Side (PM) Size D O T F 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.
6 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 F Hydrostatic Drive Oil 130 F F, earig ube Oil 120 F F ube Oil ircuits 110 F F. VISOSITY OETION 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
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