OR STAINLESS STEEL CONSTRUCTION
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1 FLUID COOLING Shell & Tube Series 92 COPPER/STEEL OR STAINLESS STEEL CONSTRUCTION Features API/BASCO Interchange ASME Code Option Preferred for New Oil-Water Applications C-Series / SSC Series Rugged Steel Construction Low Cost Type 316 Stainless Steel Construction Optional Custom Designs Available Competitively Priced Optional Material Construction on C-Series: Tubes, Tubesheets, End Bonnets NPT, SAE O-Ring, SAE Flange, or BSPP Shell Side Connections Available End Bonnets Removable for Servicing Mounting Feet Included (May be rotated in 90 increments) Ratings Standard Maximum Shell Pressure 300 psi Maximum Tube Side Pressure 150 psi Maximum Temperature 300 F Ratings ASME Code Maximum Shell Pressure 300 psi Maximum Tube Side Pressure 150 psi ASME Code SSC psi Maximum Temperature 300 F How to Order Model Series CS & SSCS CM & SSCM CF CFM Model Size Selected Baff le Spacing Materials C Series Tubes Copper Headers Steel Shell Steel Shell Connections Steel Baff les Brass End Bonnets Cast Iron Mounting Brackets Steel Gaskets Nitrile Rubber/Cellulose Fiber Nameplate Aluminum Foil Tube Diameter Code 4-1/4 6-3/8 C = NPT Shell side connections; NPT Tube side connections CS = SAE O-Ring Shell side connections; NPT Tube side connections CM = BSPP Shell side connections; BSPP Tube side connections CF = SAE Flange (with UNC threads) Shell side connections; NPT Tube side connections CFM = SAE Flange (with Metric threads) Shell side connections; BSPP Tube side connections SSC = NPT Shell side connections; NPT Tube side connections SSCS = SAE O-Ring Shell side connections; NPT Tube side connections SSCM = BSPP Shell side connections; BSPP Tube side connections Tubeside Passes 0 - One Pass T - Two Pass F - Four Pass TTPSales@thermasys.com Cooling Tube Material Blank - Copper CN - CuNi SS - Stainless Steel AD - Admiralty Brass Materials SSC Series Tubes 316 Stainless Steel Tubesheets 316 L Stainless Steel Shell 316 L Stainless Steel Shell Connections 316 L Stainless Steel Baff les 316 Stainless Steel End Bonnets 316 Stainless Steel Mounting Brackets Mild Steel Gaskets Nitrile Rubber/Cellulose Fiber Nameplate Aluminum Foil + End Bonnet Material Blank - Cast Iron B - Bronze SB - Stainless Steel Tubesheet Material Blank - Steel W - CuNi S - Stainless Steel Zinc Anodes Blank - None Z - Zinc ADD FOR C, CS, CM, CF and CFM MODELS ONLY: Cooling tube material, end bonnet material, tubesheet material & zinc anodes Consult factory for ASME Code
2 Dimensions One Pass All Models except C-600 Series C-600 Series Flange Size GG HH Z - CF Z - CFM /8-16 UNC M /2-13 UNC M /8-11 UNC M-16 NOTE: We reserve the right to make reasonable design changes without notice. Consult factory. All dimensions are inches. TTPSales@thermasys.com
3 Dimensions Two Pass C-600, C-1000, C-1700 Series C-800, C-1200 Series Flange Size GG HH Z - CF Z - CFM /8-16 UNC M /2-13 UNC M /8-11 UNC M TTPSales@thermasys.com NOTE: We reserve the right to make reasonable design changes without notice. Consult factory. All dimensions are inches.
4 Dimensions Four Pass All Models except C-1700 Series C-1700 Series Flange Size GG HH Z - CF Z - CFM /8-16 UNC M /2-13 UNC M /8-11 UNC M-16 NOTE: We reserve the right to make reasonable design changes without notice. Consult factory. All dimensions are inches. TTPSales@thermasys.com
5 Performance Curves Ship Wt. Model (lbs) F F F F F F F F F F F F F F F F F F F F F F F F F F F F F F F F F F 300 * Shipping Weights are approximate
6 Selection Procedure Performance Curves are based on 100SSU oil leaving the cooler 40 F higher than the incoming water temperature (40 F approach temperature). Curves are based on a 2:1 oil to water ratio. Step 1 Step 2 Step 3 Step 4 Step 5 Determine the Heat Load. This will vary with different systems, but typically coolers are sized to remove 25 to 50% of the input nameplate horsepower. (Example: 100 HP Power Unit x.33 = 33 HP Heat load.) If BTU/Hr. is known: HP = BTU/Hr 2545 Determine Approach Temperature. Desired oil leaving cooler F Water Inlet temp. F = Actual Approach Determine Curve Horsepower Heat Load. Enter the information from above: HP heat load x 40 x Viscosity = Curve Actual Approach Correction A Horsepower Enter curves at oil flow through cooler and curve horsepower. Any curve above the intersecting point will work. Determine Oil Pressure Drop from Curves. Multiply pressure drop from curve by correction factor B found on oil viscosity correction curve. = 5 PSI; = 10 PSI; = 20 PSI; = 40 PSI. Oil Temperature Oil coolers can be selected by using entering or leaving oil tempertures. Typical operating temperature ranges are: Hydraulic Motor Oil 110 F F Hydrostatic Drive Oil 130 F F Lube Oil Circuits 110 F F Automatic Transmission Fluid 200 F F Desired Reservoir Temperature Return Line Cooling: Desired temperature is the oil temperature leaving the cooler. This will be the same temperature that will be found in the reservoir. Off-Line Recirculation Cooling Loop: Desired temperature is the temperature entering the cooler. In this case, the oil temperature change must be determined so that the actual oil leaving temperature can be found. Calculate the oil temperature change (Oil T) with this formula: Oil T=(BTU s/hr.)/gpm Oil Flow x 210). To calculate the oil leaving temperature from the cooler, use this formula: Oil Leaving Temperature = Oil Entering Temperature - Oil T. This formula may also be used in any application where the only temperature available is the entering oil temperature. Oil Pressure Drop: Most systems can tolerate a pressure drop through the heat exchanger of 20 to 30 PSI. Excessive pressure drop should be avoided. Care should be taken to limit pressure drop to 5 PSI or less for case drain applications where high back pressure may damage the pump shaft seals. Maximum Flow Rates Example Model No F Unit Baff le Shell Side Tube Side (GPM) Size Spacing (GPM) O T F , 3 19, , 4 32, , 5 41, , 6 60, , , Exceptions to Maximum Shell Side Flows * 63 GPM Max * 33 GPM Max * 66 GPM Max * 105 GPM Max * 200 GPM Max. Caution: Incorrect installation can cause this product to fail prematurely, causing the shell side and tube side fluids to intermix. Piping Hook-up Specific applications may have different piping arrangements. Contact factory for assistance. TTPSales@thermasys.com
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