1 for the gas compositions given below, design a line heater for a well flowing at 17 MMsed into a Ine heater at an inlet pressure of 1200 psig after choking, The pas line heater has a choke at the entrance with a single coil downstream. Assume at the wellhead that flowing tubing pressure is 4500 psie and temperature is 1300. A gas condensate is produced at a rate of 30.0b6l/MMsc with a specific gravity of 0.81. Find the total beater duty required for a single 3 in XX coil downstream of choke, minimum colllength and fire tube area for a required heat flux of 10000 btu/hit. Suggest heater sie(shell diameter, shell length, fire tube rating, coll length, and number of passes). Assume constant water bath temperature of 1950F. Note: the pas stream was initially saturated with brine (3% salinity under reservoir conditions of 6000 psa and 1670F. Use Fl: 2011 in the text for estimating the overall heat transfer coefficient U). Mole Component 79.63 methane 8.76 ethane 423 propane 0.94 Isobutane 1.05 normal butane 046 Isopentane 0.46 normal pentane 0.92 hestane 1.91 heptane plus 0.39 carbon dioxide 0.00 hydrogen sulphide 1.35 rogen