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Desulfurization of hydrocarbon feed comprises adsorbing sulfur compounds in adsorption column that acts as simulated moving bed and distilling raffinate and extract

机译:烃类进料的脱硫包括在用作模拟移动床的吸附塔中吸附硫化合物,并蒸馏提余液和萃取液。

摘要

The desulfurization of a hydrocarbon feed with a boiling range of 150-450[deg]C and a sulfur content of up to 3% comprises adsorbing sulfur compounds from the feed in an adsorption column that acts as a simulated moving bed, distilling the raffinate to produce a desulfurized gas oil stream and a desorbent recycle stream for the adsorption column, and distilling the extract to produce a sulfur-containing impurity stream and a desorbent recycle stream for the adsorption column. The desulfurization of a hydrocarbon feed with a boiling range of 150-450[deg]C and a sulfur content of up to 3% comprises adsorbing sulfur compounds from the feed (1) in an adsorption column (2) that acts as a simulated moving bed and comprises several adsorbent beds with different selectivities for sulfurized and unsulfurized hydrocarbons and comprises a first zone between a inlet for desorbent (9b) and an outlet for extract (4), a second zone between the extract outlet and feed inlet, a third zone between the feed inlet and an outlet for raffinate (3) and a fourth zone between the raffinate outlet and the desorbent inlet, distilling the raffinate in a distillation column (5) to produce a desulfurized gas oil stream (8) and a desorbent recycle stream (9) for the adsorption column, and distilling the extract in a distillation column (6) to produce a sulfur-containing impurity stream (10) and a desorbent recycle stream (11) for the adsorption column.
机译:沸程为150-450℃且硫含量最高为3%的烃类进料的脱硫包括将进料中的硫化合物吸附在用作模拟移动床的吸附塔中,将提余液蒸馏为产生用于吸附塔的脱硫瓦斯油流和解吸剂再循环流,并蒸馏提取物以产生用于吸附塔的含硫杂质流和解吸剂再循环流。沸程为150-450℃且硫含量最高为3%的烃类进料的脱硫包括将来自进料(1)的硫化合物吸附在吸附塔(2)中,该模拟操作床,包括几个对硫化和未硫化的烃具有不同选择性的吸附剂床,并包括位于解吸剂入口(9b)和萃取液出口(4)之间的第一区,萃取液出口与进料口之间的第二区,第三区在进料入口与萃余液出口(3)之间以及萃余液出口与解吸剂入口之间的第四区之间,在蒸馏塔(5)中蒸馏萃余液以产生脱硫瓦斯油料流(8)和解吸剂再循环料流(9)用于吸附塔,并将萃取物在蒸馏塔(6)中蒸馏以产生用于吸附塔的含硫杂质流(10)和解吸剂再循环流(11)。

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