A natural gas pipeline is operating at a pressure of 500 psia. The pipeline gas has a viscosity of 0.0115 cP and density of 1.926 lb/ft3. The pipe is 1 schedule 80 steel. The flowmeter for the pipeline has failed but the gas pressure drop is 85.0 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?