A compressor undergoes a reversible, steady flow process. The gas at inlet and outlet of the compressor is designated as state 1 and state 2 respectively. Potential and kinetic energy changes are to be ignored. The following notations are used: v = specific volume and P = pressure of the gas. The specific work required to be supplied to the compressor for this gas compression process is
(a) $\int_{1}^{2} pdv$ (b) $\int_{1}^{2} vdp$
(c) v1(P2–P1) (d) –p2(v1–v2)