Separation of olefins from olefins/paraffins mixed gas

摘要

A method and apparatus for the separation of C4 olefins (butene-1, trans-2-butene, cis-2-butene, etc.) and C4 paraffins (normal butane, isobutane, etc) from a C4 hydrocarbon mixed gas including butene-1, trans-2-butene, cis-2-butene, normal butane, isobutane, etc. is provided. The apparatus includes several adsorption towers loaded with an adsorbent which selectively adsorb olefins and two distillation towers for the separation of the mixture gases of olefins/desorbents and paraffins/desorbents respectively. The basic operating process of the adsorption tower comprises an adsorption step of selectively adsorbing C4 olefin from the feeding mixture, a C4 olefin rinse step of removing a small amount of C4 paraffins adsorbed together with C4 olefins, and a desorption step of desorbing C4 olefins by using a desorbent, and further comprises pressure equalization step, concurrent depressurization step, and accumulation pressure step to increase the yield and concentration of olefins depending on the operation pressure of the adsorption tower.

主权项

1. An apparatus for separating C4 olefins from a mixture gas of C4 olefins/paraffins by carrying out repeated sequential adsorbing, rinsing and desorbing in such a way of performing displacement desorption using desorbents, in adsorption towers loaded with adsorbents which selectively adsorb olefins and a distillation tower for the separation olefins/desorbents and a distillation tower for the separation of paraffins/desorbents that separate the mixture gas recovered from the adsorption towers by using desorbents,
wherein the adsorption tower is configured to include: an adsorption tower (AD-1) that is connected with a feeding conduit (1) that feeds the mixture gas of C4 oleffins/paraffins, a C4 olefins/desorbents discharging conduit (2) that is connected with a distillation tower (D2), a conduit (3) that feeds a predetermined amount of C4 olefins from the distillation (D2), a conduit (4) that guides the paraffins/desorbents discharged at the rinsing to the distillation tower (D1), a conduit (5) that feeds the paraffins/desorbents discharged at the adsorbing to the distillation tower (D1), and a conduit (6) that is fed with desorbents separated from the distillation towers D1 and D2); an adsorption tower (AD-2) that is connected with a feeding conduit (1) that feeds the mixture gas of C4 olefins/paraffins, a C4 olefins/desorbents discharging conduit (2) that is connected with a distillation tower (D2), a conduit (3) that feeds a predetermined amount of C4 olefins from the distillation (D2), a conduit (4) that guides the paraffins/desorbents discharged at the rinsing to the distillation tower (D1), a conduit (5) that feeds the paraffins/desorbents discharged at the adsorbing to the distillation tower (D1), and a conduit (6) that is fed with desorbents separated from the distillation towers (D1 and D2); and an adsorption tower (AD-3) that is connected with a feeding conduit (1) that feeds the mixture gas of C4 olefins/paraffins, a C4 olefins/desorbents discharging conduit (2) that is connected with a distillation tower (D2), a conduit (3) that feeds a predetermined amount of C4 olefins from the distillation (D2), a conduit (4) that guides the araffms/desorbents discharged at the rinsing to the distillation tower D1), a conduit(5) that feeds the paraffins/desorbents discharged at the adsorbing to the distillation tower (D1), and a conduit (6) that is fed with desorbents separated from the distillation towers (D1 and D2), and wherein the paraffins/desorbents distillation tower is the distillation tower (D1) that separates the C4 paraffins and desorbents from the adsorption towers (AD-1, AD-2, and AD-3) and the olefins/desorbents distillation tower is the distillation tower (D2) that separates the C4 olefins and desorbents from the adsorption towers (AD-1 AD-2, and AD-3).