In the present work, numerical simulation has been done to analyze transien
ts in gas flow and pressure in a horizontal straight pipe. For a single gas
pipeline, eight representative cases corresponding to different causes of
transient behaviour are simulated to predict unsteady state flow and the ev
olution of pressure profiles. The numerical results show that depending upo
n the pipe dimensions and operating variables such as pressure and gas flow
rate, transient effects in the pipeline may last for a long time and/or ov
er significant length of pipe. The simulations predict an initial surge in
gas flow rate greater than the final steady-state value if the pressure dro
p across the pipe is increased. Similarly, initial flow rate may decrease b
elow the final steady-state value if the pressure drop is decreased. In cas
e of complete closure of a valve, oscillations in both pressure and mass fl
ow rate are observed, which gradually decay and the steady state conditions
of no flow are ultimately achieved. The present results are compared with
a published work from the literature. A reasonably good agreement is found
between these two predictions. The present study is of practical significan
ce in safe design and operation of a gas delivery system.