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Piping diagrams, Selection procedure – Thermal Transfer Systems K Series User Manual

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K

[email protected]

262.554.8330

www.thermaltransfer.com

82

W

A

T

E

R C
O

O

L

E

D

K

Piping Diagrams

Single Pass Model

Two Pass Model

A = Hot fluid to be cooled
B = Cooled fluid
C = Cooling water in
D = Cooling water out

Selection Procedure

Performance Curves are based on 100SSU oil leaving the cooler 40°F
higher than the incoming water temperature (40°F approach temperature).

Step 1

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

Step 2

Determine Approach temperature.

Desired oil leaving cooler °F – Water Inlet temp. °F = Actual
Approach

Step 3

Determine Curve Horsepower Heat load. Enter the

information from above:
HP heat load x 40 x Viscosity = Curve

Actual Approach Correction A Horsepower

Step 4

enter curves at oil flow through cooler and curve horsepower.

Any curve above the intersecting point will work.

Step 5

Determine oil pressure Drop from Curves. Multiply pressure

drop from curve by correction factor B found on oil viscosity
correction curve.
l

= 5 PSI; n = 10 PSI; s = 20 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 - 130°F

Hydrostatic Drive Oil

130°F - 180°F

Lube Oil Circuits

110°F - 130°F

Automatic Transmission Fluid

200°F - 300°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.

C

B

A

D

B

A

C

D

C

B

A

D

B

A

C

D

50 60 70 80 90100

150

200 250 300

400 500

.5

.6

.7

.8

.9

1

2

3

4

5

1.5

2.5

OIL VISCOSITY CORRECTION MULTIPLIERS

OIL VISCOSITY - SSU

VISCOSITY CORRECTION

A

B