Liquid phase adsorptive separation of cycloparaffins from hydrocarbon mixture

1. A process for separating one or more one-ring cycloparaffins and one or more multi-ring cycloparaffins from a hydrocarbon mixture, the process comprising the steps of:

providing the hydrocarbon mixture; and

contacting the hydrocarbon mixture with an adsorbent material comprising a metal organic framework to separate at least a portion of the one or more one-ring cycloparaffins and the one or more multi-ring cycloparaffins from the hydrocarbon mixture, the metal organic framework being selected from the group consisting of zirconium-based metal organic framework, hafnium-based metal organic framework, cerium-based metal organic framework, titanium-based metal organic framework, or a combination thereof,

wherein the process is conducted in a liquid phase.

2. The process of claim 1 , wherein the hydrocarbon mixture comprises one or more n-paraffins, one or more iso-paraffins, one or more one-ring cycloparaffins, and one or more multi-ring cycloparaffins.

3. The process of claim 2 , wherein the process generates a first eluate comprising at least a portion of the one or more n-paraffins and at least a portion of the one or more iso-paraffins and a second eluate comprising the at least a portion of the one or more one-ring cycloparaffins and one or more multi-ring cycloparaffins.

4. The process of claim 3 , wherein generating the first eluate and the second eluate further comprises desorbing using a solvent.

5. The process of claim 4 , wherein the solvent is a saturated hydrocarbon, an aromatic hydrocarbon, or mixtures thereof.

6. The process of claim 4 , wherein the solvent is iso-octane, hexane, toluene, benzene, CO 2 , ammonia, or mixtures thereof.

7. The process of claim 2 , wherein the process comprises separating one or more one-ring cycloparaffins, and one or more two-ring cycloparaffins from the hydrocarbon mixture.

8. The process of claim 7 , wherein the one or more one-ring cycloparaffins comprise one or more cyclohexanes, and one or more two-ring cycloparaffins comprise one or more decalins.

9. The process of claim 1 , wherein the hydrocarbon mixture comprises one or more aromatic hydrocarbons, one or more n-paraffins, one or more iso-paraffins, one or more one-ring cycloparaffins, and one or more multi-ring cycloparaffins.

10. The process of claim 9 , wherein the process generates a first eluate comprising the one or more n-paraffins and the one or more iso-paraffins and a second eluate comprising one or more aromatic hydrocarbons, the one or more one-ring cycloparaffins, and the one or more multi-ring cycloparaffins.

11. The process of claim 1 , wherein the process is performed between about 1 bar to about 100 bar.

12. The process of claim 1 , wherein the process is performed between about 25° C. and about 250° C.

13. The process of claim 1 , wherein the metal organic framework is a zirconium-based metal organic framework.

14. The process of claim 13 , wherein the zirconium-based metal organic framework exhibits an X-ray diffraction pattern containing peaks at d-spacings of about 11.98 Å, 10.37 Å, 7.32 Å, 6.24 Å, 5.98 Å, and 5.18 Å.

15. The process of claim 13 , wherein the zirconium-based metal organic framework comprises Zr 6 O 32 clusters bridged by polytopic, carboxylate-based linkers.

16. The process of claim 13 , wherein the zirconium-based metal organic framework comprises a micropore volume, as measured by N 2 adsorption at 77 K, greater than 0.38 cc/g.

17. The process of claim 13 , wherein the zirconium-based metal organic framework comprises a residual inorganic mass after combustion of the zirconium-based metal organic framework that is greater than about 45% of dry weight of zirconium-based metal organic framework measured at 300° C.

18. The process of claim 13 , wherein the zirconium-based metal organic framework can be represented by a general formula Zr 6 O 4 (OH) 4 BDC (6-x) , wherein BDC refers to benzene-1,4-dicarboxylate, and wherein x is greater than 0.5 as determined by residual inorganic mass after combustion.

19. The process of claim 1 , wherein the adsorbent material comprises about 10% metal organic framework and about 90% binder.

20. The process of claim 1 , wherein the metal organic framework is prepared using a defect modulator selected from the group consisting of acetic acid, formic acid, benzoic acid, trifluoroacetic acid, difluoroacetic acid, fluoroacetic acid, trichloroacetic acid, dichloroacetic acid, chloroacetic acid, and an alkyl derivative of acetic acid.

21. A process for separating one or more one-ring cycloparaffins and one or more multi-ring cycloparaffins from a hydrocarbon mixture, the process comprising the steps of:

providing the hydrocarbon mixture; and

contacting the hydrocarbon mixture with an adsorbent material comprising a metal organic framework to separate at least a portion of the one or more one-ring cycloparaffins and one or more multi-ring cycloparaffins from the hydrocarbon mixture by selectively retaining the at least a portion of the one or more one-ring cycloparaffins and the one or more multi-ring cycloparaffins,

wherein the process is conducted in a liquid phase, and

wherein the metal organic framework comprises a metal organic framework prepared using a defect modulator.