Benzene → Cumene

HRID 19426

Reaktionsgleichung

Reaktionsgleichung von HRID 19426
[CH:1]1[CH:6]=[CH:5][CH:4]=[CH:3][CH:2]=1.[CH2:7]([C:9]1C=CC=CC=1)[CH3:8]>O>[C:1]1([CH:7]([CH3:9])[CH3:8])[CH:6]=[CH:5][CH:4]=[CH:3][CH:2]=1

Komponenten

4

Reagenzien, Katalysatoren, Lösungsmittel 1

Versuchsvorschrift

The benzene column 140 receives feed from the bottoms of the depropanizer column 130 in the line 136 after it is mixed with transalkylation effluent in a line 152. The benzene column 140 produces a benzene column overhead stream comprising benzene in a line 142 and a benzene column bottom stream comprising ethylbenzene and PEBs in a line 144. The overhead benzene stream in the line 142 may be provided with a water concentration of about 50 to about 150 wppm and a temperature of at least about 120° C. and preferably greater than 125° C. and no more than about 170° C. The depropanizer intermediate stream in the line 132 has similar properties, and is combined with stream 142 and delivered to a hot adsorbent vessel 160 by line 161. The hot adsorbent vessel 160 contains a bed of acidic molecular sieve adsorbent for the removal of ONCs, including nitrites from the mixed benzene stream in the line 161. The denitrogenated benzene effluent in a line 164 is delivered to both the alkylation reactor 120 by the line 102 and to a transalkylation reactor 150 by a line 166. The benzene stream in the line 166 is mixed with an intermediate stream comprising diisopropylbenzene (DIB) in a line 168 from a heavies column 190. The mixture of benzene and DIB in a line 154 are delivered to the transalkylation reactor 150. The DIB transalkylates with benzene over a transalkylation catalyst bed 156 in the transalkylation reactor 150 to produce cumene. Transalkylation effluent in the line 152 has a greater concentration of cumene and a smaller concentration of benzene and DIB than in the line 154.

Aufarbeitung

  1. additionis mixed with transalkylation effluent in a line 152
  2. customof at least about 120° C. and preferably greater than 125° C. and no more than about 170° C
  3. customdelivered to a hot adsorbent vessel
  4. customfor the removal of ONCs
  5. additionThe benzene stream in the line 166 is mixed with an intermediate stream comprising diisopropylbenzene (DIB) in a line 168 from a heavies column 190
  6. additionThe mixture of benzene and DIB in a line 154

Quellen und Nachweise

ORD-Eintrag
ord-37a15b509f9b414ead6c5fa90296f766
Quelldatensatz
uspto-grants-2010_06
Patentnummer
US07744828B2

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