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402 SECTION    III Applications


            in the range of approximately 0.2MPa (in the case of blowers) to 19MPa in the
            case of barrel compressors.”
               Refinery process gases can be corrosive, such as sour crude, which has a
            high sulfur content. Corrosive gases cause damage to the compressor flow path
            and seals over time. Compressors in refinery applications are typically installed
            outdoors unless extreme temperature environments require indoor installations.
            The benefit of an outdoor installation is that there is lower explosion risk and the
            installation cost is reduced by avoiding indoor safety requirements of gas mon-
            itoring, fire suppression, and room-air cycling.


            LNG Production

            The International LNG trade is expanding at a rapid pace with LNG accounting
            for approximately 9%–10% of global gas supply. Table 10.1 provides some
            salient parameters of the current LNG market.
               Converting natural gas to LNG is accomplished by chilling and liquefying
            the gas to a temperature of 113K. When liquefied, the volume of the natural gas
            is reduced to 1/600th of its standard volume. This allows the efficient transpor-
            tation of gas using specialized LNG tankers. The size of a liquefaction facility is
            usually stated in millions of tons per annum (MTPA). One metric ton of LNG is
            equivalent to 54.8 GJ of gas. The refrigeration is accomplished using several
            commercially available processes that typically involve the successive chilling
            of the feed gas to lower temperatures using mechanical refrigeration systems
            utilizing large refrigeration compressors. The compressors are typically driven
            by gas turbines ranging from 30 to 120MW.
               LNG compressors include the following:

            l main refrigeration compressors
            l boil of gas compressors
            l end flash compressors
            l regeneration compressors


              TABLE 10.1 LNG Market

              Parameter                                 Value
              Global LNG trade in 2016                  258 MT
              Global nominal liquefaction capacity      340 MTPA
              LNG shipping fleet                        439 ships
              Share of LNG in global gas supply         9.8%
              Data from IGU World LNG Report (2017) https://www.igu.org/sites/default/files/103419-World_
              IGU_Report_no%20crops.pdf.
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