If the compressor outlet (or tank inside ) temp and pressure remain constant AND the bag inner surface does not transfer much heat (which is probably true for the short time you are stating---
U = internal inergy Kj
m = mass kg
H = enthalpy kj
p= pressure N/sq meter
V = volume cu. meters
energy balance of the air bag yields
dU = ho dm - pdV
dH - pdV -Vdp = ho dm -p dV ho is stagnation enthalpy of source (tank, compressor) and next will be assumed constant.
integration yields H - Hi - integ Vdp = ho (m-mi)
where subscript i relates to initail conditions in bag.
mh - mi* hi - integ Vdp = ho (m-mi)
mi, hi, pi, should be known. Problem is to integrate Vdp
Let us assuume mi in bag is negligible
mh - integ Vdp = ho* m
or m(h-ho) = integ Vdp
m and integ Vdp will be positive numbers.
Therefore h - ho = positive number and final specific enthalpy will increase within bag.
For a perfect gas, the temp within bag will increase.
Regards