Liquefied natural gas (LNG) is attracting great interest
as a clean
energy alternative to other fossil fuels, mainly due to its ease of
transport and low carbon dioxide emissions, a primary factor in air
pollution and global warming. It is expected that this trend in the
use of LNG will lead to steady increases in demand over the next few
decades. To meet the growing demand for LNG, natural gas liquefaction
plants have been constructed across the globe. Furthermore, single
train capacity has been increased to strengthen price competitiveness.
To achieve greater capacity, more complex refrigeration cycle designs
that combine two or more different conventional single refrigeration
cycles are being developed to obtain synergistic effects in the liquefaction
process. At the same time, a variety of recent studies have focused
on designing suitable processes for offshore and small-scale plants
to improve the profitability of stranded gas fields. LNG plants are
known to be energy/cost-intensive, as they require a large amount
of power for the processes of compression and refrigeration, and need
special equipment such as cryogenic heat exchangers, compressors,
and drivers. Therefore, one of the primary challenges in the LNG industry
is to improve the efficiency of the current natural gas liquefaction
processes in combination with cost savings. In this paper, we review
recent developments in LNG processes, with an emphasis on commercially
available refrigeration cycles. We also discuss recent research and
suggest future directions for natural gas liquefaction processes.
Up to this point, most studies have focused on operating cost. To
achieve better results, future studies that investigate optimal design
and operation of LNG technologies should consider both capital cost
and operating cost.
-Natural gas liquefaction process runs under cryogenic condition, and it spends large amount of energy. Minimizing energy consumption of natural gas liquefaction process is an important issue because of its physical characteristics. Among many kinds of natural gas liquefaction processes, C3-MR(Propane Pre-cooled Mixed Refrigerant) process uses two kind of refrigerants. One is the propane as the pure refrigerant(PR) and the other is the mixed refrigerant(MR). In this study, to find the optimal compressing level, propane cycle is simulated on different pressure level. The case study result shows relationship between energy consumption and pressure level. As a result, the conclusion is that at a higher pressure level, process consumes lower energy. At 5 pressure-levels, energy consumption is 23.7% lower than 3 pressure-levels.
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