Aromatic production apparatus
One exemplary embodiment can include an aromatic production apparatus. The aromatic production apparatus can include a first fractionation zone, a second fractionation zone, and a third fractionation zone. Generally, the first fractionation zone can provide a stream rich in an aromatic C8 − and a stream rich in an aromatic C9, the second fractionation zone can separate at least one of benzene and optionally toluene from a transalkylation zone effluent and provide a feed to the first fractionation zone, and the third fractionation zone can receive the stream rich in the aromatic C8 − from the first fractionation zone. An effluent from the third fractionation zone can be directly comprised in a para-xylene-separation zone feed to a para-xylene-separation zone.
1. An aromatic production apparatus, comprising:
a) a first fractionation zone for providing a stream rich in an aromatic C8 − and a stream rich in an aromatic C9;
b) a second fractionation zone for separating at least one of benzene and optionally toluene from a transalkylation zone effluent and providing a feed to the first fractionation zone; and
c) a third fractionation zone for receiving the stream rich in the aromatic C8 − from the first fractionation zone wherein an effluent from the third fractionation zone is directly comprised in a para-xylene-separation zone feed to a para-xylene-separation zone.
2. The aromatic production apparatus according to claim 1 , wherein the second fractionation zone comprises a benzene column and a toluene column.
3. The aromatic production apparatus according to claim 1 , wherein the first fractionation zone comprises a column providing the stream rich in the aromatic C8 − as a top stream and the stream rich in the aromatic C9 as a bottom stream.
4. The aromatic production apparatus according to claim 1 , wherein the first fractionation zone comprises a column providing the stream rich in the aromatic C8 − as a top stream, the stream rich in the aromatic C9 as a side stream, and a bottom stream rich in an aromatic C10 + .
5. The aromatic production apparatus according to claim 1 , further comprising a transalkylation zone adapted to receive at least a portion of the stream rich in the aromatic C9.
6. The aromatic production apparatus according to claim 5 , wherein the first fractionation zone comprises a column providing the stream rich in the aromatic C8 − as a top stream, the stream rich in the aromatic C9 as a side stream, and a bottom stream rich in an aromatic C10 + .
7. The aromatic production apparatus according to claim 6 , further comprising:
an alkylaromatic isomerization zone adapted to receive at least a portion of the para-xylene-separation zone effluent from the para-xylene-separation zone; and
an extraction zone providing at least a portion of an extraction zone effluent to the second fractionation zone.
8. An aromatic production apparatus, comprising:
a) a naphtha hydrotreating zone;
b) a reforming zone receiving an effluent from the naphtha hydrotreating zone;
c) an extraction zone receiving a first fraction from the reforming zone; and
d) a para-xylene-separation zone receiving a second fraction from the extraction zone and a transalkylation zone via a first fractionation zone and a second fractionation zone; wherein
i) the first fractionation zone for providing a stream rich in an aromatic C8 − and a stream rich in an aromatic C9 wherein the first fractionation zone is communicated directly with the transalkylation zone and an aromatic gasoline blend to provide at least a portion of the stream rich in the aromatic C9 to the transalkylation zone or the aromatic gasoline blend; and
ii) the second fractionation zone comprises a benzene column and a toluene column wherein a bottom stream from the toluene column is provided to the first fractionation zone.