10
Chemical Technology • March 2016
Heat integration with power plant
Simple cycle power plant
W
heretheregasificationplantislocatedclosetoapowerplant,
a hybrid type systemusingwaste heat fromthe gas turbine
and Submerged Combustion Vaporisers (SCVs) for LNG
heating can increase the thermal efficiency of the integrated facility.
The heat integration scheme for a simple cycle power plant can
be illustrated as shown in Figure 7. In this configuration, hot water
is used as an intermediate fluid. The circulating water is heated by
the hot exhaust gas from the gas turbine in a direct contact heating
tower. When waste heat recovery is operated, the fuel gas burners
of the SCVs are not required; the LNG vaporisation duty is supplied
by the circulating hot water.
Fuel firing with SCVs is only required when the power plant is
not operating or when the quantity of waste heat is insufficient to
support the regasification duty.
With the use of waste heat, there are significant energy savings, in
addition to the reduction in CO
2
and NOx emissions from the facility.
In addition, the chilled water from the LNG plant can be used to
lower the gas turbine inlet temperature using an exchanger. This
is particularly advantageous when operating during hot summer
days when the gas turbine output typically drops due to higher
ambient temperature. Lowering the gas turbine inlet temperature
can significantly increase the power output as shown in Figure 8.
Typically, for each degree centigrade drop in air temperature,
power output can be increased by 0,7 to 1,2 % depending on the
gas turbine aerodynamic design characteristics. Typically, aero-
derivative gas turbines are designed with a higher compression
ratio and higher efficiency than industrial gas turbines, and would
benefit more with inlet air chilling, as shown in Figure 8.
Combined cycle power plant
For combined cycle power plants, low pressure steam is condensed
in the surface condenser in the steam cycle using cooling water.
The cooling water return can be used to supply heating to the
LNG plant as shown in Figure 9. This integration method
is cur-
rently employed in the large Grain CHP station to increase thermal
efficiency and reduce emissions. The thermal efficiency of an
Part 1 of this article appeared in the August
2015 issue of
Chemical Technology
. Today’s
LNG landscape is changing. Many of the newer
LNG import terminals are smaller in size and
are mainly located in South East Asia and South
America. These new terminals place a strong
emphasis on energy efficiency, environmental
impacts and emissions.
LNG
vaporisers selection
based on site ambient conditions – Part 2
by John Mak, Senior Fellow and Technical Director,
Nick Amott, Curt Graham, Dhirav Patel, Fluor, USA
Figure 7: Simple cycle power plant integration