Methods and systems for producing para-xylene from C8-containing compositions
A method for producing para-xylene (PX) includes introducing a C8 aromatic-containing composition to a xylene rerun column to separate the C8 aromatic-containing composition into a xylene-containing effluent and a heavy effluent and passing the xylene-containing effluent to a PX processing loop that includes a PX recovery unit operable to separate a PX product from the xylene-containing effluent, a membrane isomerization unit operable to convert a portion of the MX, OX, or both from the xylene-containing effluent to PX, an EB dealkylation unit operable to dealkylate EB from the xylene-containing effluent to produce benzene, toluene, and other C 7− compounds, and a membrane separation unit operable to produce a permeate that is PX-rich and a retentate that is PX-lean. The permeate is passed to the PX recovery unit for recovery of PX, which the retentate is bypassed around the PX recovery unit circulated through the xylene processing loop.
1. A system for producing para-xylene (PX) from a C8 aromatic-containing composition, the system comprising:
a xylene rerun column operable to separate the C8 aromatic-containing composition into a xylene-containing effluent and a heavy effluent, the xylene-containing effluent comprising at least PX and one or more of ortho-xylene (OX), meta-xylene (MX), ethylbenzene (EB), or combinations of these;
a xylene processing loop comprising:
a PX recovery unit disposed directly downstream of the xylene rerun column so that the xylene-containing effluent passes directly from the xylene rerun column to the PX recovery unit, where the PX recovery unit is operable to separate the xylene-containing effluent into at least a PX product and a PX-depleted effluent;
a membrane isomerization unit disposed directly downstream of the PX recovery unit so that the PX-depleted effluent passes directly from the PX recovery unit to the membrane isomerization unit, the membrane isomerization unit operable to convert at least a portion of the MX, OX, EB, or combinations of these from the xylene-containing effluent to PX;
a membrane separation unit disposed downstream of the membrane isomerization unit and operable to separate at least a portion of the xylene-containing effluent into a permeate that is PX-rich and a retentate that is PX-lean, where the permeate is recycled back to the PX recovery unit; and
an ethylbenzene dealkylation unit disposed downstream of the membrane separation unit so that the retentate passes directly from the membrane separation unit to the ethylbenzene dealkylation unit, the ethylbenzene dealkylation unit operable to dealkylate at least a portion of the EB from the xylene-containing effluent to produce one or more C 7− compounds.
2. The system of claim 1 , further comprising a stripper disposed directly downstream of the EB dealkylation unit, the stripper operable to remove at least a portion of the one or more C 7− compounds from the xylene processing loop.
3. The system of claim 1 , in which the membrane isomerization unit comprises an acidic sulfonated catalytic membrane.
4. The system of claim 1 , in which the membrane separation unit comprises a carbon-based membrane.
5. The system of claim 2 , where the stripper is operable to separate a dealkylation effluent from the ethylbenzene dealkylation unit into a C 7− effluent, an EB-depleted effluent, and a stripper bottoms, where the stripper bottoms is recycled back to the xylene rerun column.