“…However, if applied at the exit of the hydroisomerization unit, the ideal target is the separation of linear and monobranched hydrocarbons from multibranched ones, as it would increase the efficiency of the whole process by recycling both low-octane linear and monobranched hydrocarbons to the head of the unit and yield a multibranched product-enriched raffinate with a high ON. Several materials have been studied and patented for this purpose, out of which silicalite-1 (Si-MFI) and other materials with MFI structure have been most frequently considered. ,− Other zeolites with diverse structures, such as AFI, AEL, ATO, BEA, FAU, FER, , ATS, CFI, , EUO, MWW, NES, ,,, MEL, MRE, and MTT, have been patented for this separation as well, but none of them clearly surpasses Si-MFI . Recently, pure silica zeolites Si-STW and EMM-17 and MOF Fe 2 (BDP) 3 (BDP 2– = 1,4-benzenedipyrazolate), have been proposed as promising adsorbents for this separation.…”