Page 301 - Hydrocarbon Exploration and Production Second Edition
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288                                                     Oil and Gas Processing


             The LNG is shipped in well-insulated tankers as a very cold liquid at boiling
          point (typically  1601C) under close to atmospheric pressure, where it occupies
          1/600th of the volume of the corresponding vapour at standard conditions. A minor
          amount of evaporation takes place during transport, but this helps cool the bulk
          of the gas in each tank aboard the ship (this process is termed ‘autorefrigeration’).
          The gas that evaporates is captured and used as fuel for the tanker vessel. LNG is not
          explosive in its liquid state, but needs to expand to a gas and mix with air in a ratio
          of 5 to 15% before an explosion can occur.
             The LNG is transported to a receiving terminal where the LNG is unloaded and
          converted back into a gaseous phase before being distributed through pipelines to
          the customers. LNG plants require very high initial investment in the order of
          several billion dollars, and are therefore only viable in cases where large volumes of
          reserves (typically 5–10 trillion cubic feet [tcf ]) have been proven. In the past, the
          overall costs of LNG processing and transportation have been significant barriers to
          widespread development, but rising energy demand and increasing energy prices
          have stimulated the construction of numerous new LNG ‘trains’ and regasification
          plants in several countries. Both developing and industrialised countries are building
          LNG regasification plants in order to diversify their energy supply and increase
          energy security.
             Overall LNG demand is forecast to grow three-fold from 2006 to 2020, from
          160 million to around 500 million tons/year. The main suppliers are Indonesia,
          Malaysia, Brunei, Australia, Trinidad, Algeria and Qatar, with new liquefaction
          plants under construction or recently on stream in, for example Egypt, Nigeria,
          Oman, Norway and Russia. The number of LNG reception terminals is also
          increasing, with several new regasification plants already built or under construction
          in, for example Great Britain, Canada, USA, Spain, China and India, with the result
          that there is now an emerging global spot market in LNG. A further development is
          floating LNG facilities, whereby a complete LNG plant is built on a vessel in order
          to bring the facilities to the gas deposits, which would be a viable scenario for
          stranded gas accumulations, or regions where there is an absence of gas
          infrastructure and/or no local gas market (Figure 11.22).


          11.1.4.4. Gas to liquids
          Gas to liquids (GTL) technology has been available for a long time, but has
          challenging economic hurdles. GTL provides an alternative method for
          commercialising stranded or remote gas resources, in addition to well-established
          technologies like LNG plants and gas pipelines. Shell has had a GTL plant in
          operation at Bintulu, Malaysia since 1993.
             The term GTL conversion refers to a group of processes that convert natural
          GTL fuels, which are easier and cheaper to transport, market and distribute.
          Another advantage of GTL is that the products contain less pollutants and fine
          particulates than conventional liquid fuels, and have a better energy yield (higher
          cetane number) resulting in improved engine performance.
             In theory virtually any hydrocarbon can be synthesised from any other, and since
          the 1920s several processes have emerged that can be used to produce synthetic
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