natural gas

please solve it

100 MMScfd of an associated gas is avarlable at 100 psia and 20F above the dew point temperature Ine gas is compressed to 400psia, cooled and chilled to 40F to recover some condensate. The residue gas is Then transported 100 miles away to be necived in the othen end at 200 psia. Fig(1) shows a simple flire sheet. 1) Explaine how to design the compression unit using a s.mple flow sheet fien the process showing all the process conditions (P,T). 2) Calculate the hossepower nequired for onc stage assuming polytropic operation. 3) The ainount of liquid produced. 4) The rate of propane nequired in the chiller if propane enters as a saturated liquid and leaves as a saturated vapor at 30F. 5) The size of the pipeline nequired to transport the residue gas