Problem 5.2.4

 

Estimate the heat loss due to free convection from a 2 feet-wide square plate that is at 130 degrees Fahrenheit to ambient air at 70 degrees Fahrenheit when it is in (a) vertical position and (b) horizontal position. 

 

Solution: 

 

(See Problem 5.2.1 also). The film temperature is 100 degrees Fahrenheit and the properties of air at this temperature are listed as: viscosity 0.0491 pound per foot per hour, density 0.071 pounds per cubic foot, thermal conductivity 0.0156 BTU per hour per foot per degree Fahrenheit, and specific heat 0.24 BTU per pound per degree Fahrenheit.

 

Beta, coefficient of thermal expansion, for ideal gases is given as 1 over T where T is the absolute temperature.  It can be found to be equal to 0.00168 per degree Rankine.  Acceleration due to gravity is 32.174 ft per second squared or 4.17 times 108 foot per hour squared.  Note that the DT is 130 minus 70 equals 60 degrees Fahrenheit.

 

With these values, Grashof number is calculated to be 7.479 times 108, whereas Prandtl number is 0.755.  This gives a value of Raleigh number as 5.649 times 108.  Nusselt number is given as aYb. 

 

(a) For square plate in vertical position, value of parameter a equals 0.59 and b equals 0.25 (See Perry, Table 10.1).  Nusselt number is calculated as 90.96.  Nusselt number is h L over k.  In this case, L is replaced by d and the heat transfer coefficient is determined to be 0.709 BTU per hour per foot squared per degree Fahrenheit. 

 

Heat transfer area is given by L2, where L is the plate characteristic length.  Actual heat transfer area is twice this area.  Heat transfer is given as h 2A DT or 340.55 BTU per hour. 

 

(b) For square plate in horizontal (FU, hot surface facing upward), value of parameter a equals 0.14 and b equals 0.333 (See Perry, Table 10.1).  Nusselt number is calculated as 114.96.  Nusselt number is h L over k.  In this case, L is replaced by d and the heat transfer coefficient is determined to be 0.897 BTU per hour per foot squared per degree Fahrenheit. 

Heat transfer is given as h 2A DT or 430.4 BTU per hour.  Note there is another correlation when hot surface is facing downwards and abbreviated as FD.