Selective sorbents for purification of hydrocartons
View Patent ↗A method for removing thiophene and thiophene compounds from liquid fuel includes contacting the liquid fuel with an adsorbent which preferentially adsorbs the thiophene and thiophene compounds. The adsorption takes place at a selected temperature and pressure, thereby producing a non-adsorbed component and a thiophene/thiophene compound-rich adsorbed component. The adsorbent includes either a metal or a metal ion that is adapted to form π-complexation bonds with the thiophene and/or thiophene compounds, and the preferential adsorption occurs by π-complexation. A further method includes selective removal of aromatic compounds from a mixture of aromatic and aliphatic compounds.
1. A process for removing at least one of thiophene and thiophene compounds from liquid fuel, the process comprising the step of:
contacting the liquid fuel with a dehydrated adsorbent which preferentially adsorbs the at least one of thiophene and thiophene compounds, at a selected temperature and pressure, thereby producing a non-adsorbed component and a thiophene/thiophene compound-rich adsorbed component, wherein the dehydrated adsorbent is dehydrated via a pretreatment process which includes heating an adsorbent at about 350° C., and wherein the dehydrated adsorbent comprises at least one of a metal and a metal ion, the at least one of metal and metal ion adapted to form π-complexation bonds with the at least one of thiophene and thiophene compounds, and wherein the preferential adsorption occurs by π-complexation.
2. The process as defined in claim 1 wherein the dehydrated adsorbent comprises a carrier having a surface area, the carrier having a monolayer of a d-block transition metal compound dispersed on at least some of the surface area, the metal compound releasably retaining the thiophene/thiophene compounds; and the carrier comprising a plurality of pores having a pore size greater than the effective molecular diameter of the thiophene/thiophene compounds; and wherein the process further includes changing at least one of the pressure and temperature to thereby release the thiophene/thiophene compound-rich component from the dehydrated adsorbent.
3. The process as defined in claim 1 wherein at ambient temperature and 10 −5 atm vapor pressure, the dehydrated adsorbent adsorbs more than 1 mmol/gram of the at least one of thiophene and thiophene compounds.
4. The process as defined in claim 2 wherein at ambient temperature and 10 −5 atm vapor pressure, the dehydrated adsorbent adsorbs more than 1 mmol/gram of the at least one of thiophene and thiophene compounds.
5. The process as defined in claim 1 wherein the dehydrated adsorbent comprises an ion-exchanged zeolite selected from the group consisting of zeolite X, zeolire Y, zeolite LSX, and mixtures thereof, the zeolite having exchangeable cationic sites, wherein the at least one metal and metal ion is a d-block transition metal cation, and wherein at least some of the sites have d-block transition metal cation present.
6. The process as defined in claim 5 wherein the dehydrated adsorbent is at least one of Cu(I)Y zeolite and Ag(I)Y zeolite.
7. The process as defined in claim 1 wherein the pretreatment process further comprises cooling the adsorbent.
8. The process as defined in claim 1 wherein the selected temperature and pressure is ambient temperature and ambient pressure.
9. The process as defined in claim 1 wherein the liquid fuel is at least one of unleaded gasoline and diesel fuel.
10. The process as defined in claim 2 wherein the dehydrated adsorbent carrier is silica and wherein the metal compound is silver nitrate.
11. The process as defined in claim 5 wherein at ambient temperature and 10 −5 atm vapor pressure, the dehydrated adsorbent adsorbs more than 1 mmol/gram of the at least one of thiophene and thiophene compounds.
12. The process as defined in claim 1 wherein the at least one of a metal and a metal ion is selected from Ni 2+ , Cu + , Pd 2+ , and Ag + .