Process for the removal of nitrogen compounds from various organic media

Claim 2

A process for effecting the removal of undesirable nitrogenous compounds from liquid organic media comprising contacting said organic media under removal conditions at a temperature below the boiling point of the organic media with a solid sorbent wherein said sorbent is selected from the group consisting of crystalline and amorphous forms of silica, bauxite, X and Y zeolites, alumina, silica-alumina and mixtures of silica and alumina having an effective amount of from about 0.001-20 weight percent of an anhydrous acid gas selected from the group consisting of hydrogen bromide and hydrogen chloride adsorbed therein until substantially all of said undesirable compounds are removed from said organic media.

Claim 3

The process of claim 1 where the sorbent has a surface area of from about 5 to about 1000 m 2 /gm and a pore diameter of from about 3 to about 200 Angstroms and wherein the amount of anhydrous acid adsorbed thereon is from about 0.1 wt. % to about 17.5 wt. %.

Claim 4

The process of claim 2 where the sorbent is an amorphous form having an average pore diameter from about 20 to about 100 Angstroms and a surface area of from about 150 to 600 m 2 /gm.

Claim 5

The process of claim 3 where the sorbent is selected from the group consisting of silica, alumina, bauxite, silica-alumina and silica and mixtures of alumina.

Claim 6

The process of claim 4 where the sorbent is an amorphous silica-alumina having from about 5 to about 95 wt. % silica.

Claim 7

The process of claim 2 where the sorbent is a crystalline zeolite form having a surface area of from about 100 to about 700 m 2 /gm and an average pore diameter of from 3-9A.

Claim 8

The process of claim 6 where the sorbent is selected from X and Y zeolites.

Claim 9

The process of claim 7 where said sorbent is a NaX zeolite.

Claim 10

The process of claim 1 where a crystalline sorbent as described therein for removing said nitrogeneous compounds is regenerated comprising (1) contacting said sorbent in the absence of water with a suitable low boiling solvent selected from naphthas, hexane, benzene and low boiling hydrocarbon distillates at atmospheric pressure and at a temperature below the boiling point of the solvent and (2) purging said sorbent with an inert gas at a temperature above the boiling point of said solvent until no solvent remains thereon; (3) then contacting said crystalline sorbent with a volatile anhydrous base and heating at a temperature of from about 450°-550° C. in a stream of inert gas for about 8-16 hours or until salt vapor emission stops; (4) thereafter contacting said sorbent with an amount of steam, air or oxygen in an amount sufficient to remove substantially all oxidizable matter from the sorbent at a temperature of from about 500°-700° C.; (5) and then contacting the sorbent with anhydrous acid gas under ambient conditions of temperature and pressure until a sufficient amount of from about 0.001-20 wt. % of said anhydrous gas effective to remove said undesirable nitrogenous compounds from said liquid organic media is resorbed therein.

Claim 11

The process of claim 9 where approximately 0.1 to about 17.5 wt. %, based on the total weight of the sorbent composition, of anhydrous acid gas is resorbed.

Claim 12

The process of claim 10 where the anhydrous acid gas resorbed is hydrogen chloride.

Claim 13

The process of claim 11 where the amount of hydrogen chloride resorbed is about 15-20 wt. %.

Claim 14

The process of claim 1 wherein an amorphous sorbent as described therein for removing said nitrogenous compounds is regenerated comprising (1) contacting said sorbent with a suitable low boiling solvent selected from light boiling naphthas, hexane, benzene and low boiling distillates at a temperature below the boiling point of said solvent and under atmospheric pressure for about 10-24 hours at a LHSV of about 0.5; (2) purging the solvent-extracted amorphous sorbent with an inert gas saturated with water vapor or dry steam at atmospheric pressure and a temperature of from about 450°-550° C. at a rate of about 500 volumes of inert gas per volume of sorbent for about 2-24 hours; and (3) then contacting the sorbent with anhydrous acid gas under ambient conditions of temperature and pressure until an amount of from 0.001 to 20 wt. % based on the total weight of the sorbent of said anhydrous acid gas effective to remove undesirable nitrogenous compounds from liquid organic media is resorbed thereby.

Claim 15

The process of claim 13 where the anhydrous acid gas resorbed is hydrogen chloride.

Claim 16

The process of claim 14 where the amount of hydrogen chloride resorbed is about 1 wt. %.

Claim 17

The process of claim 13 wherein said solvent extracted amorphous sorbent prior to contacting said anhydrous acid gas is purged with air or oxygen at a temperature of 500°-700° C. to remove substantially all oxidizable matter therefrom.

Claim 18

The process of claim 13 where approximately 0.01 to about 17.5 wt. %, based on the total weight of the sorbent composition of anhydrous acid gas is resorbed.

Claim 19

The process of claim 1 where the organic media is a liquid hydrocarbon.

Claim 20

The process of claim 2 where the hydrocarbon is an oil of lubricating viscosity.

Claim 21

The process of claim 1 where the anhydrous acid gas is hydrogen chloride.

Claim 22

A process for effecting the removal of undesirable nitrogenous compounds from liquid organic media containing same comprising contacting said organic media at atmospheric pressure or slightly higher and at a temperature of from ambient to about 5° C. below the boiling point of the organic media with (1) a suitable dehydrating or drying agent, (2) a solid sorbent selected from the group consisting of crystalline and amorphous forms of sorbents selected from the group consisting of silica, bauxite, alumina, silica-alumina and mixtures of silica and alumina and X and Y zeolites having an amount of from 0.001 to 20 wt. % based on the total weight of the sorbent of an anhydrous acid gas selected from the group consisting of hydrogen bromide and hydrogen chloride adsorbed therein effective to remove said nitrogenous compounds and (3) with a crystalline sorbent not having been sorbed with said acid gas.

Claim 23

A process for effecting the removal of undesirable nitrogenous compounds from liquid organic media containing same comprising contacting said organic media at atmospheric pressure or slightly higher and at a temperature of from ambient to about 5° C. below the boiling point of the organic media with (1) a suitable dehydrating or drying agent, (2) a solid sorbent selected from the group consisting of crystalline and amorphous forms of sorbents selected from the group consisting of silica, bauxite, alumina, silica-alumina and mixtures of silica and alumina and X and Y zeolites having an amount of from 0.001 to 20 wt. % based on the total weight of the sorbent of an anhydrous acid gas selected from the group consisting of hydrogen bromide and hydrogen chloride adsorbed therein effective to remove said nitrogenous compounds and (3) with a crystalline sorbent not having been sorbed with said acid gas.

Claim 24

The process of claim 21 where the dehydrating agent and the crystalline sorbent not sorbed with acid gas are zeolite molecular sieves.

Claim 25

The process of claim 22 where the crystalline sorbent is NaX zeolites.