To 25362 : I cannot follow your calculation but there are probably 2 reasons for this. The first is that I am not at home in your units. I guess the number 10 is the specific heat of water in BTU/gallon.F, but I don't know what the 30 represents. The second, and more important reason, is that I am not sure that I understand esimp2k's question.
The title of the thread hints that there are two streams entering the tank, but the wording of the actual query makes it look like the combining they are talking of is the single entering stream plus what is already in the tank.
If we were talking of 2 separate streams entering the tank and creating an average temperature of 120F then the volume of the tank would be irrelevant. All that is required is that the two streams are well mixed. As the question specifically asks for the volume of the tank I must conclude that we are not talking about combining two entering streams.
If we are looking at a single stream entering a tank at 180F and the overflow (effluent) from the tank leaving at 120F then the heat can only go to one place, i.e. that it is lost through the tank walls to the atmosphere. I presume also that we are looking at a steady state question i.e. we are not trying to calculate how long it takes for the tank to get to 120F.
What we really need to calculate then is how much heat is entering the tank (in the 180F water) and how much wall area we need to be able to get this heat out of the tank. The tank has to be at 120F (given) so the heat entering the tank relative to this is simply (mass flow x specific heat x temperature change)
Assuming the 20 gpm are US gallons the flowrate is 10,000 lb/h. The specific heat of water is 1 btu/lb.F and the temperature change is 60 F (i.e. 180 - 120). The heat entering the tank is therefore 10,000 x 1 x 60 = 600,000 btu/h.
The heat transfer from the tank walls will depend on the tank material of construction, the air velocity around the tank etc, so it is impossible to say anything other than that the heat transfer coefficient will be low, probably less than 2 btu/h.ft2.F. Assuming an ambient temperature of 70F gives a temperature difference of 120-70=50F. This gives an area of 600,000 / (2 x 50) = 6,000 ft2. Assuming a cube shaped tank and no heat transfer out of the top or bottom faces, the area of each face is 1,500 ft2. This gives an edge of virtually 40 ft.
If the assumption of a single stream flowing in at 180 F is correct then a cubic tank 40x40x40 ft would be required. The volume is therefore about 480,000 US gallons, but will depend on the actual heat transfer conditions around the tank. Putting a cooling coil in the tank, or a heat exchanger on the effluent will be a more practical solution.
Harvey
Katmar Software
Engineering & Risk Analysis Software