Liquefied Natural Gas (LNG)

After the recovery of natural gas liquids, sweet dry natural gas may be liquefied for transportation through cryogenic tankers. Further treatment may be required to reduce the water vapor below 10 ppm and carbon dioxide and hydrogen sulfide to less than 100 and 50 ppm, respectively.  Two methods are generally used to liquefy natural gas: the expander cycle and mechanical refrigeration. In the expander cycle, part of the gas is expanded from a high transmission pressure to a lower pressure. This lowers the temperature of the gas. Through heat exchange, the cold gas cools the incoming gas, which in a similar way cools more incoming gas until the liquefaction temperature of methane is reached. Figure 1  is a flow diagram for the expander cycle for liquefying natural gas.

      Figure 1. Flow diagram of the expander cycle for liquefying natural gas:

(1) pretreatment (mol.sieve), (2) heat exchanger, (3) turboexpander.

  In mechanical refrigeration, a multicomponent refrigerant consisting of nitrogen, methane, ethane, and propane is used through a cascade cycle. When these liquids evaporate, the heat required is obtained from natural gas, which loses energy/temperature till it is liquefied. The refrigerant gases are recompressed and recycled. Figure 2  shows the MCR natural gas liquefaction process.

Figure2. The MCR process for liquefying natural gas:15 (1) coolers, (2) heat

exchangers, (3,4) two stage compressors, (5) liquid-vapor phase separator.

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