首页> 外国专利> The diisopropylbenzene (DIPB), toriisopuropirubenzen (TIPB) and manner in order to separate DIPB and TIPB from the feed which includes poly alkylate heavy ones

The diisopropylbenzene (DIPB), toriisopuropirubenzen (TIPB) and manner in order to separate DIPB and TIPB from the feed which includes poly alkylate heavy ones

机译:二异丙基苯(DIPB),甲苯基异硫氰酸双苯酯(TIPB)以及从包含多烷基化重烃的进料中分离出DIPB和TIPB的方法

摘要

Processes and apparatuses for separating diisopropylbenzene (DIPB) and triisopropylbenzene (TIPB) from a feed (21) comprising DIPB, TIBP and polyalkylate heavies are disclosed. The disclosed processes include introducing the feed (21) into a distillation column (22) having a column top (24) pressure of less than 35 kPa (5 psia), a column bottoms (25) pressure of less than 21 kPa (3 psi), and preferably 14 kPa (2 psi) or less above the column top pressure with a bottoms temperature ranging from 224 to 241 C (435 to 465F). The processes also include taking OFF a side draw (28) comprising at least 99.8 wt% of the DIPB and at least 50 wt% of the TIPB present in the feed (21) and a bottoms stream (41) comprising at least 95 wt% of the heavies contained in the distillation feed (21). The low temperature bottoms temperature enables high pressure steam to be used as the bottoms reboiler (38) HEAT source.
机译:公开了从包含DIPB,TIBP和聚烷基化物重质的进料(21)中分离二异丙基苯(DIPB)和三异丙基苯(TIPB)的方法和设备。公开的方法包括将进料(21)引入蒸馏塔(22),该蒸馏塔的塔顶(24)压力小于35kPa(5psia),塔底(25)压力小于21kPa(3psi)。 ),并且最好比塔顶压力高14 kPa(2 psi)或更低,塔底温度范围为224至241 C(435至465 F)。该方法还包括排出包含在进料(21)中的至少99.8重量%的DIPB和至少50重量%的TIPB的侧馏分(28)和包含至少95重量%的塔底料流(41)。蒸馏进料(21)中所含的重组分低温塔底温度使高压蒸汽可用作塔底再沸器(38)HEAT源。

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