Liquefied natural gas (LNG) is being
imported in Pakistan to bridge
the gap between the indigenous production and demand for natural gas.
The calorific value of imported LNG must be lowered to meet the design
requirements of the existing gas-fired power plants. This reduction
in calorific value requires mixing with high-purity nitrogen, which
can be obtained from the cryogenic distillation of air. Because imported
LNG has a significant amount of cold energy and must be regasified/vaporized
before injecting into the gas pipeline network, there is potential
for recovering this cold energy by integrating the LNG regasification
process with the cryogenic air separation process. To achieve these
objectives, we developed an integrated LNG regasification–air
separation process and compared it with the standalone air separation
process. Conventional exergy analysis shows that the integrated process
is better than the standalone air separation process both in terms
of total power consumption and total exergy destruction ratio. The
integrated process was further analyzed using advanced exergy analysis
to identify the origin and nature of exergy destruction in the process.
The results show that 44.3% of total exergy destruction in the process
can be classified as avoidable. Moreover, 91.7% of the avoidable exergy
destruction is of endogenous nature, showing that improving the efficiency
of individual pieces of equipment should be the topmost priority for
process improvement.