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CALCULATION OF BLEVE CONDITIONS FOR
CARBON DIOXIDE
BLEVEs
are very unusual but extremely catastrophic events that can occur with carbon
dioxide under pressure. The last really bad explosion with carbon dioxide
occurred some time ago in Worms, Germany. Since then carbon dioxide had been
stored cool at atmospheric pressure. BLEVEs also occur with other gases,
notably with propane at higher temperatures, usually as a result of fire.
However,
now that carbon dioxide and its mixtures are being used under pressure for gas
and oil recovery, carbon capture and storage and supercritical fluid processes,
BLEVE must again be considered. This involves calculating the range of
conditions of pressure and temperature where BLEVEs can occur. Even under these
conditions a BLEVE is unlikely but, because of the enormity of BLEVE explosions,
it is prudent to avoid these conditions. In fact failure to avoid BLEVE
conditions is quite inconsistent with the current safety culture in oil and gas
companies.

There
have been a number of reported BLEVEs with carbon dioxide, mostly involving
fire extinguishers. However, one of the most catastrophic examples was the
explosion of a tank of CO2 at a plant in Worms, Germany in 1988. A
tank of 30 tonne capacity was shattered into a number of pieces and only 20% of
the tank was present in the original premises after the explosion. Most of the
tank was propelled 300 metres into the Rhine. There were three fatalities and a
further eight casualties. The premises containing the tank originally were
devastated. The event is reported in: W.E. Clayton and M.L. Griffin,
‘Catastrophic failure of a liquid carbon dioxide storage vessel’ Process
Safety Progress, 1994, 13, 202-209. (Their Figure 5 is above)
Why
do BLEVEs occur? A theory developed by Professor Reid and colleagues at MIT
(M.E. Kim and R.C. Reid, ‘ The rapid depressurization of hot, high pressure
liquids or supercritical fluids’ in Chemical engineering at supercritical
fluid conditions, edited by M.E. Paulaitis, Ann Arbor Science, 1983) shows
that a very spectacular physical event must occur under certain circumstances,
and this is likely to be the explanation of BLEVEs. A simplified explanation of
this theory can be given with the aid of the figure below, which is a diagram
of the relationship between the pressure in a substance and the volume it
occupies as a liquid, gas and fluid.

The
continuous thick black line ABCD shows the behaviour of the substance at
a constant temperature and at thermodynamic equilibrium. In the section AB,
the substance is a liquid and as the volume it occupies is expanded the
pressure falls dramatically. Eventually the pressure falls to the vapour
pressure of the liquid at the particular temperature at B. The liquid
then starts to evaporate to become a liquid-gas mixture, and the pressure stays
constant at the vapour pressure. Eventually it reaches C, where the
liquid has been completely converted to gas. The pressure then drops as it is
expanded further.
However,
if the pressure falls suddenly, due to a failure in the container, the
substance can become an unstable liquid along the path BS, coloured red.
Along the path BS the substance is metastable and can at any time boil
to return to the equilibrium horizontal line BC. Although such an event
can be very violent is not thought to be a BLEVE. Typically violent boiling
will occur before the point S is reached and a BLEVE will not occur.
However,
in the unlikely event that the point S is reached a special and
catastrophic situation arises. S is known as a spinodal point and
the slope of the line at this point is zero (i.e.
). The dotted red line connects these points at different
temperatures and is known as the spinodal curve, which ends at the
critical point. The special nature of situations represented by points along
this curve are that large density fluctuations can occur because of the
insensitivity of pressure to volume (
).
Once
the spinodal curve is reached separation into liquid and gas must occur.
The density variations develop spontaneously into liquid and gas regions. This
occurs homogeneously throughout the whole liquid. The rise in pressure on to
the vapour pressure line BC is not large but it happens at great speed,
homogeneously and at time scale of molecular motion. The shock to the
containing vessel is huge and a disastrous BLEVE happens.

For a BLEVE to occur, the substance has therefore to
find itself on the spinodal curve between 1 bar and the critical point where
the curve ends. When a catastrophic failure occurs there is not time for heat
to pass into the system and so the path during failure is adiabatic. In
thermodynamic terms the entropy of the system is constant during failure and
this allows the conditions for BLEVE to be calculated. It can be shown that for
CO2 the temperature-pressure conditions must be within the red
envelope shown in the figure. For other gases and gas mixtures the envelope
will be different, but again can be calculated. These envelopes should be
prudently avoided
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