N-paraffin purification process with removal of aromatics

A method of removing co-boiling aromatic hydrocarbons using a bed of a solid sorbent in a process for separating normal paraffinic hydrocarbons from a feed stream of normal paraffinic hydrocarbons, isoparaffinic hydrocarbons, and co-boiling aromatic hydrocarbons, wherein said co-boiling aromatic hydrocarbons have boiling points within the boiling point range of said normal paraffinic hydrocarbons, which method comprises the steps of:

• a) passing a paraffin-feed stream comprising an isoparaffinic hydrocarbon having more than 6 carbon atoms per molecule, a normal paraffinic hydrocarbon having the same number of carbon atoms as said isoparaffinic hydrocarbon, and a co-boiling aromatic hydrocarbon to a fixed first bed of a solid first sorbent containing a first compound, sorbing said normal paraffinic hydrocarbon and said co-boiling aromatic hydrocarbon within a paraffin sorption zone within said first sorbent of said first bed, and withdrawing a paraffin-raffinate stream comprising said isoparaffinic hydrocarbon and said first compound from said first bed;
• b) passing a paraffin-desorbent stream comprising said first compound to said first bed at a different point than said paraffin-feed stream is passed to said first bed, desorbing said normal paraffinic hydrocarbon and said co-boiling aromatic hydrocarbon from said first sorbent within a paraffin desorption zone within said first bed, and withdrawing a paraffin-extract stream comprising said normal paraffinic hydrocarbon, said co-boiling aromatic hydrocarbon, and said first compound from said first bed at a different point than said paraffin-raffinate stream is withdrawn from said first bed;
• c) simulating the utilization of a moving bed of said first sorbent by maintaining a net fluid flow through said first bed and by periodically moving in a unidirectional pattern the points at which said paraffin-feed stream and said paraffin-desorbent stream are passed to said first bed and the points at which said paraffin-extract stream and said paraffin-raffinate stream are withdrawn from said first bed to gradually shift the location of said paraffin sorption and paraffin desorption zones within said first bed;
• d) passing at least a portion of said paraffin-extract stream to an aromatics removal zone comprising a fixed second bed of a solid second sorbent in a aromatic sorption step, desorbing a second compound from said second bed while sorbing said co-boiling aromatic hydrocarbon within said second bed, and withdrawing from said aromatics removal zone a first product stream comprising said normal paraffinic hydrocarbon, a first recycle stream comprising said first compound, and a second recycle stream comprising said second compound;
• e) passing at least a portion of said paraffin-raffinate stream to a first separation zone, and recovering from said first separation zone a second product stream comprising said isoparaffinic hydrocarbon and said co-boiling aromatic hydrocarbon, a third recycle stream comprising said first compound, and a fourth recycle stream comprising said second compound;
• f) passing an aromatic-desorbent stream comprising at least a portion of at least one of said second recycle stream and said fourth recycle stream to a fixed third bed of said solid second sorbent in an aromatic desorption step, desorbing said co-boiling aromatic hydrocarbon within said third bed while sorbing said second compound within said third bed, and withdrawing therefrom an aromatic-extract stream comprising said co-boiling aromatic hydrocarbon and said second compound;
• g) passing at least a portion of said aromatic-extract stream to said first separation zone;
• h) recovering at least a portion of at least one of said first recycle stream and said third recycle stream as said paraffin-desorbent stream;
• and
• i) periodically interchanging said second and said third fixed beds in said aromatic sorption and aromatic desorption steps.

A method of removing co-boiling aromatic hydrocarbons using a bed of a solid sorbent in a process for separating normal paraffinic hydrocarbons from a feed stream of normal paraffinic hydrocarbons, isoparaffinic hydrocarbons, and co-boiling aromatic hydrocarbons, wherein said co-boiling aromatic hydrocarbons have boiling points within the boiling point range of said normal paraffinic hydrocarbons, which method comprises the steps of:

• a) passing a paraffin-feed stream comprising an isoparaffinic hydrocarbon having more than 6 carbon atoms per molecule, a normal paraffinic hydrocarbon having the same number of carbon atoms as said isoparaffinic hydrocarbon, and a co-boiling aromatic hydrocarbon to a paraffin sorption zone within a fixed first bed of a solid first sorbent containing normal pentane and isooctane, sorbing said normal paraffinic hydrocarbon and said co-boiling aromatic hydrocarbon within a paraffin sorption zone within said first sorbent of said first bed, passing para-xylene from a paraffin flushing zone within said first bed to said paraffin sorption zone, and withdrawing a paraffin-raffinate stream comprising said isoparaffinic hydrocarbon, normal pentane, isooctane, and para-xylene from said first bed;
• b) passing a paraffin-flush stream comprising isooctane and para-xylene to said first bed at a different point than said paraffin-feed stream is passed to said paraffin flushing zone of said first bed, and flushing said isoparaffinic hydrocarbon from the interstitial void volume of said first bed within said paraffin flushing zone within said first bed;
• c) passing a paraffin-desorbent stream comprising normal pentane and isooctane to said first bed at a different point than said paraffin-feed stream and said paraffin-flush stream are passed to said first bed, desorbing said normal paraffinic hydrocarbon and said co-boiling aromatic hydrocarbon from said first sorbent within a paraffin desorption zone within said first bed, and withdrawing a paraffin-extract stream comprising said normal paraffinic hydrocarbon, said co-boiling aromatic hydrocarbon, normal pentane, isooctane, and para-xylene from said first bed at a different point than said paraffin-raffinate stream is withdrawn from said first bed;
• d) simulating the utilization of a moving bed of said first sorbent by maintaining a net fluid flow through said first bed and by periodically moving in a unidirectional pattern the points at which said paraffin-feed stream, said paraffin-flush stream, and said paraffin-desorbent stream are passed to said first bed and the points at which said paraffin-extract stream and said paraffin-raffinate stream are withdrawn from said first bed to gradually shift the location of said paraffin sorption, paraffin flushing, and paraffin desorption zones within said first bed;
• e) passing said paraffin-extract stream to a fixed second bed of a solid second sorbent in an aromatic sorption step, desorbing para-xylene from said second bed while sorbing said co-boiling aromatic hydrocarbon within said second bed, and withdrawing from said second bed an aromatic-raffinate stream comprising said normal paraffinic hydrocarbon, normal pentane, isooctane, and para-xylene;
• f) passing said aromatic-raffinate stream to a first separation zone and recovering from said first separation zone a first overhead stream comprising normal pentane and isooctane, a first sidecut stream comprising normal pentane, isooctane, and para-xylene, and a first bottom stream comprising said normal paraffinic hydrocarbon;
• g) passing said paraffin-raffinate stream to a second separation zone, and recovering from said second separation zone a second overhead stream comprising normal pentane and isooctane, a second sidecut stream comprising normal pentane, isooctane, and para-xylene, and a second bottom stream comprising said isoparaffinic hydrocarbon and said co-boiling aromatic hydrocarbon;
• h) passing said first sidecut stream and said second sidecut stream to a third separation zone and recovering from said third separation zone a third overhead stream comprising normal pentane and isooctane and a third bottom stream comprising isooctane and para-xylene;
• i) passing said third overhead stream to said second separation zone;
• j) passing a first portion of said third bottom stream to a fixed third bed of said solid second sorbent in an aromatic desorption step, desorbing said co-boiling aromatic hydrocarbon within said third bed while sorbing para-xylene within said third bed, and withdrawing from said third bed an aromatic-extract stream comprising isooctane, paraxylene, and said co-boiling aromatic hydrocarbon;
• k) passing said aromatic-extract stream to said second separation zone;
• l) recovering a second portion of said third bottom stream as said paraffin-flush stream for Step (b);
• m) passing a first portion of a combined stream comprising said first overhead stream in Step (f) and said second overhead stream in Step (g) to a fixed fourth bed of said solid second sorbent in an aromatic flushing step, flushing said normal paraffinic hydrocarbon from the interstitial void volume of said fourth bed, and withdrawing an aromatic-flush effluent stream comprising normal pentane, isooctane and said normal paraffinic hydrocarbon;
• n) passing said aromatic-flush effluent stream to said first separation zone;
• o) recovering a second portion of said combined stream as said paraffin-desorbent stream for Step (c);
• and
• p) periodically changing said second fixed bed in said aromatic sorption step to said fourth fixed bed in said aromatic flushing step, periodically changing said fourth fixed bed to said third fixed bed in said aromatic desorption step, and periodically changing said third fixed bed to said second fixed bed.

A method of removing co-boiling aromatic hydrocarbons using a bed of a solid sorbent in a process for separating normal paraffinic hydrocarbons from a feed stream of normal paraffinic hydrocarbons, isoparaffinic hydrocarbons, and co-boiling aromatic hydrocarbons, wherein said co-boiling aromatic hydrocarbons have boiling points within the boiling point range of said normal paraffinic hydrocarbons, which method comprises the steps of:

• a) passing a paraffin-feed stream comprising an isoparaffinic hydrocarbon having more than 6 carbon atoms per molecule, a normal paraffinic hydrocarbon having the same number of carbon atoms as said isoparaffinic hydrocarbon, and a co-boiling aromatic hydrocarbon to a paraffin sorption zone within a fixed first bed of a solid first sorbent containing a normal pentane and isooctane, sorbing said normal paraffinic hydrocarbon and said co-boiling aromatic hydrocarbon within a paraffin sorption zone within said first sorbent of said first bed, passing para-xylene from a paraffin flushing zone within said first bed to said paraffin sorption zone, and withdrawing a paraffin-raffinate stream comprising said isoparaffinic hydrocarbon, normal pentane, isooctane, and para-xylene from said first bed;
• b) passing a paraffin-flush stream comprising isooctane and para-xylene to said first bed at a different point than said paraffin-feed stream is passed to said paraffin flushing zone of first bed, and flushing said isoparaffinic hydrocarbon from the interstitial void volume of said first bed within said paraffin flushing zone within said first bed;
• c) passing a paraffin-desorbent stream comprising normal pentane and isooctane to said first bed at a different point than said paraffin-feed stream and said paraffin-flush stream are passed to said first bed, desorbing said normal paraffinic hydrocarbon and said co-boiling aromatic hydrocarbon from said first sorbent within a paraffin desorption zone within said first bed, and withdrawing a paraffin-extract stream comprising said normal paraffinic hydrocarbon, said co-boiling aromatic hydrocarbon, normal pentane, isooctane, and para-xylene from said first bed at a different point than said paraffin-raffinate stream is withdrawn from said first bed;
• d) simulating the utilization of a moving bed of said first sorbent by maintaining a net fluid flow through said first bed and by periodically moving in a unidirectional pattern the points at which said paraffin-feed stream, said paraffin-flush stream, and said paraffin-desorbent stream are passed to said first bed and the points at which said paraffin-extract stream and said paraffin-raffinate stream are withdrawn from said first bed to gradually shift the location of said paraffin sorption, paraffin flushing, and paraffin desorption zones within said first bed;
• e) passing said paraffin-extract stream to a first separation zone and recovering therefrom a first overhead stream comprising normal pentane and isooctane, a first sidecut stream comprising normal pentane, isooctane, and para-xylene, and a first bottom stream comprising said normal paraffinic hydrocarbon and said co-boiling aromatic hydrocarbon;
• f) passing said first bottom stream to a fixed second bed of a solid second sorbent in an aromatic sorption step, desorbing para-xylene from said second bed while sorbing said co-boiling aromatic hydrocarbon within said second bed, and withdrawing from said second bed an aromatic-raffinate stream comprising said normal paraffinic hydrocarbon and para-xylene;
• g) passing said aromatic-raffinate stream to a second separation zone and recovering from said second separation zone a second overhead stream comprising para-xylene and a second bottom stream comprising said normal paraffinic hydrocarbon, and passing said second overhead stream to said first separation zone;
• h) passing said paraffin-raffinate stream to a third separation zone, and recovering from said third separation zone a third overhead stream comprising normal pentane and isooctane, a second sidecut stream comprising normal pentane, isooctane, and para-xylene, and a third bottom stream comprising said isoparaffinic hydrocarbon and said co-boiling aromatic hydrocarbon;
• i) passing said first sidecut stream and said second sidecut stream to a fourth separation zone and recovering from said fourth separation zone a fourth overhead stream comprising normal pentane and isooctane and a fourth bottom stream comprising isooctane and para-xylene;
• j) passing said fourth overhead stream to said third separation zone;
• k) passing a first portion of said fourth bottom stream to a fixed third bed of said solid second sorbent in an aromatic desorption step, desorbing said co-boiling aromatic hydrocarbon within said third bed while sorbing para-xylene within said third bed, and withdrawing from said third bed an aromatic-extract stream comprising isooctane, para-xylene, and said co-boiling aromatic hydrocarbon;
• l) passing said aromatic-extract stream to said third separation zone;
• m) recovering a second portion of said fourth bottom stream as said paraffin-flush stream for Step (b);
• n) passing a first portion of a combined stream comprising said second overhead stream in Step (e) and said third overhead stream in Step (h) to a fixed fourth bed of said solid second sorbent in an aromatic flushing step, flushing said normal paraffinic hydrocarbon from the interstitial void volume of said fourth bed, and withdrawing an aromatic-flush effluent stream comprising normal pentane, isooctane and said normal paraffinic hydrocarbon;
• o) passing said aromatic-flush effluent stream to said first separation zone;
• p) recovering a second portion of said combined stream as said paraffin-desorbent stream for Step (c);
• and
• q) periodically changing said second fixed bed in said aromatic sorption step to said fourth fixed bed in said aromatic flushing step, periodically changing said fourth fixed bed to said third fixed bed in said aromatic desorption step, and periodically changing said third fixed bed to said second fixed bed.