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thermosyphoning freeze protection 11 jul 2003 andrew swingler suggests thermosyphoning as one form of freeze protection for evacuated tube collectors above a heat storage tank. this might be the only form of freeze protection needed for freeze-tolerant heat-pipe tubes below a pressurized header with some insulation on the header and its supply and return pipes, and a pipe with minimal elbows and a circulation pump that doesn't block flow when stopped. cool water weighs about 62.67 - 0.003t lb/ft^3, with t in degrees f. the density difference caused by the temperature difference between up and down pipes causes a pressure difference proportional to the height of the water column, making water flow through the resistance of the pipe loop. with 16' of height and a dt temperature difference, dp = 0.048dt lb/ft^2. bill shurcliff says a pipe with radius r and length l in feet and pressure diff dp has laminar flow q = pir^4dp/(8mul) ft^3/s. viscosity mu is about 6x10^-7 lb-s/ft^2 for 32 f water. with, say, 32' of 1/2" pipe, 16' up and down, q = pi(0.25/12)^4dp/(8x6x10^-7x32') = 0.004dp ft^3/s or 43dt lb/h, which moves 43dt^2 btu/h. if the heat pipe collector header is 6"x6"x8' long, with 16 ft^2 of surface and r4 insulation and a 16/4 = 4 btu/h-f conductance from 60 f water temp to outdoor air at, say, -20 f, (60+20)4 = 320 btu/h makes dt = sqrt(320/43) = 2.7 f, if i did that right :-) water goes up at 60 f and returns at 57.3 f, well above 32 f. at -40, with about 400 btu/h of heat loss, the water might return at 60-sqrt(400/43) = 57.0 f. nick |