A natural gas pipeline is operating at a pressure of $500$psia$.$ The pipeline gas has a viscosity of $0\mathrm{.}0115$ cP and density of $1\mathrm{.}926$ lb$/$ft$3.$ The pipe is $1$schedule $80$ steel. The flowmeter for the pipeline has failed but the gas pressure drop is $85\mathrm{.}0$ psi$$over a distance of $10$ miles. What is the flowrate, in lb$/$h$,$ though the pipe? What is the$$compressor pumping power required to make up for the pressure drop over $10$ miles?$$