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SOLVED:Measured conditions for the bottoms from a depropanizer distillation unit in a small refinery are given below. Using the data in Figure 2.3 and assuming an ideal liquid solution (volume of mixing =0 ), compute the liquid density in lb / ft^3, lb / gal, lb / bbl (42 gal), and kg / m^3. Phase Condition Liquid Temperature, ^∘F 229 Pressure, psia 282 Flow rates, lbmol/h: C3 2.2 i C4 171.1 n C4 226.6 i C5 28.1 n C5 17.5
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