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Fischer Tropsch synthesis of syngas to liquid hydrocarbons  219






























              Figure 7.1 Schematic line-up of the integrated FT synthesis process [2]. FT,
              Fischer Tropsch.


              fixed-bed  reactor  in  1936  in  Germany   with  a  capacity  of
              B274 330 MT/day, and gasoline was the major product of the process
              and constituted 72% of the total production. Besides, the first coal-based
              production plant was constructed in Secunda, South Africa in 1955 by
              South African Coal and Oil Company due to the huge availability of coal
              in this country. Shell in Malaysia was the second earliest commercial plant
              that was producing liquid hydrocarbons using FT synthesis process, while
              circulating fluidized bed (CFB) reactors were used for world’s largest FT
              application known as “Synthol reactors” [6,7,11,12,48].
                 This chapter discusses the technical details linking to FT synthesis
              along with its recent developments and presents the current status on syn-
              gas to liquid hydrocarbons. Recently, the interest towards FT synthesis
              has increased as a result of eco-friendly concerns and the higher fossil fuels
              consumption. This chapter mainly aimed to provide a detailed summary
              of (1) FT synthesis of syngas to liquid hydrocarbons, (2) role of different
              catalysts in FT synthesis, (3) kinetic modeling and process simulation for
              FT synthesis, (4) role of carbon nanofibers (CNFs)/carbon felt (CF)
              composites, and (5) plug the knowledge gaps and provide new research
              directions to improve the FT synthesis.
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