Page 221 - Handbook of Energy Engineering Calculations
P. 221

0, 0.2, 0.4, 0.6, and 0.8 load on the engine. Plot the result as curve B, Fig. 9.
                  Perform a similar calculation for condition c—full flow through the bypass
               circuit. Plot the results as curve C, Fig. 9.


               4. Compute the actual cooling-water flow rate
               Find  the  points  of  intersection  of  the  pump  total-head  curve  and  the  three

               system head-loss curves A, B, and C, Fig. 9. These intersections occur at 314,
               325, and 330 gal/min (19.8, 20.5, and 20.8 L/s), respectively.
                  The  initial  design  assumed  a  10°F  (5.6°C)  temperature  rise  through  the
               engine  with  a  water  flow  rate  of  281  gal/min  (17.7  L/s).  Rearranging  the

               equation  in  step  1  gives  Δ  t  =  H/(400G).  Substituting  the  flow  rate  for
               condition a gives an actual temperature rise of Δt = (402)(3500)/[(500)(314)]
               = 8.97°F (4.98°C). If a 180°F (82.2°C) rated thermostatic element is used in
               the three-way valve, holding the outlet temperature t  to 180°F (82.2°C), the
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               inlet temperature t  will be Δt = t  − t  = 8.97; 180 − t  = 8.97; t  = 171.03°F
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               (77.2°C).
               5. Determine the required surge-tank capacity
               The surge tank in a cooling system provides storage space for the increase in
               volume of the coolant caused by thermal expansion. Compute this expansion
               from E = 62.4 gΔ V, where E = expansion, gal (L); g = number of gallons

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               required to fill the cooling system: Δ V = specific volume, ft /lb (m /kg) of
               the  coolant  at  the  operating  temperature  −  specific  volume  of  the  coolant,
                          3
                 3
               ft /lb (m /kg) at the filling temperature.
                  The cooling system for this engine must have a total capacity of 281 gal
               (1064 L), step 1. Round this to 300 gal (1136 L) for design purposes. The
               system operating temperature is 180°F (82.2°C), and the filling temperature

               is usually 60°F (15.6°C). Using the steam tables to find the specific volume
               of the water at these temperatures, we get E = 62.4(300)(0.01651 − 0.01604)
               = 8.8 gal (33.3 L).
                  Usual  design  practice  is  to  provide  two  to  three  times  the  required

               expansion  volume.  Thus,  a  25-gal  (94.6-L)  tank  (nearly  three  times  the
               required capacity) would be chosen. The extra volume provides for excess
               cooling  water  that  might  be  needed  to  make  up  water  lost  through  minor
               leaks in the system.
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