Process for separation of phenol and btx aromatics from gas condensates
A BTX aromatic hydrocarbon and phenol technology, applied in the field of equipment operating the process, can solve the problems of affecting the solvent extractability, inability to handle separation, and the efficiency of the extraction process is deteriorated, so as to minimize energy consumption, small size, and economical advantages. Effect
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[0055] exist figure 1 In the process flow diagram shown schematically in , gas condensate 1 released from tar and oil is introduced into an extraction zone 2 . Gaseous condensates released mainly from phenol and BTX aromatics leave the extraction plant as raffinate stream 3 and are supplied to figure 1 Further processing not shown in .
[0056] The first distillation column 5 is loaded with an organic extractant 4 loaded with phenol and BTX aromatics, here diisopropyl ether (DIPE). A phenol-rich phase is obtained as bottom product 6 , which is still loaded with residual amounts of DIPE and is charged to a second distillation column 7 . From the enrichment section 5a of the first distillation column 5 a stream 8 is withdrawn from a third theoretical tray (counting the trays from top to bottom) and is charged to a third distillation column 9 which Designed as a column with 30 theoretical trays. Stream 8 is loaded onto tray 17 of column 9 .
[0057] In the third distillation...
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