Process for the Production of Xylenes
US-2015376086-A1 · Dec 31, 2015 · US
US10759724B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10759724-B2 |
| Application number | US-201815952511-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 13, 2018 |
| Priority date | Sep 11, 2014 |
| Publication date | Sep 1, 2020 |
| Grant date | Sep 1, 2020 |
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Embodiments of the present disclosure describe a zeolite-like metal-organic framework composition comprising a metal-organic framework composition with ana topology characterized by the formula [MIII(4, 5-imidazole dicarboxylic acid)2X(solvent)a]n wherein MIII comprises a trivalent cation of a rare earth element, X comprises an alkali metal element or alkaline earth metal element, and solvent comprises a guest molecule occupying pores. Embodiments of the present disclosure describe a method of separating paraffins comprising contacting a zeolite-like metal-organic framework with ana topology with a flow of paraffins, and separating the paraffins by size.
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What is claimed is: 1. A composition, comprising: a metal-organic framework composition with ana topology characterized by the formula [M III (4, 5-imidazole dicarboxylic acid) 2 X(solvent) a ] n wherein M III comprises a trivalent cation of a rare earth element, X comprises one or more alkali metal elements or one or more alkaline earth metal elements, solvent comprises a guest molecule occupying pores, a is at least 1, and n is at least 1. 2. The composition of claim 1 , wherein M III includes one or more of any one of the following trivalent cations of a rare earth element: Ce 3+ , Dy 3+ , Er 3+ , Eu 3+ , Gd 3+ , Ho 3+ , La 3+ , Lu 3+ , Nd 3+ , Pr 3+ , Pm 3+ , Sm 3+ , Sc 3+ , Tb 3+ , Tm 3+ , Yb 3+ , or Y 3+ . 3. The composition of claim 1 , wherein X is lithium, sodium, potassium, rubidium, cesium, francium, beryllium, magnesium, calcium, strontium, barium, or radium. 4. The framework of claim 1 , wherein the metal-organic framework composition with ana topology is anionic. 5. The composition of claim 1 , wherein the pore sizes of the metal-organic framework composition with ana topology tunable to within a range of less than about 0.5 Å. 6. The composition of claim 1 , wherein the pore sizes of the metal-organic framework composition with ana topology are tuned to about 4.2 Å to 5.0 Å. 7. The composition of claim 1 , wherein the metal-organic framework composition with ana topology is one or more of a thin film membrane and a zeolite molecular sieve. 8. The composition of claim 1 , wherein the metal-organic framework composition with ana topology is an adsorbent for separating paraffins by size. 9. A method of separating paraffins, comprising: contacting a metal-organic framework with ana topology with a flow of paraffins, and separating the paraffins by size, wherein the metal-organic framework with ana topology is characterized by the formula [M III (4, 5-imidazole dicarboxylic acid) 2 X(solvent) a ] n wherein M III comprises a trivalent cation of a rare earth element, X comprises one or more alkali metal elements or one or more alkaline earth metal elements, solvent comprises a guest molecule occupying pores, a is at least 1, and n is at least 1. 10. The method of claim 9 , wherein separating paraffins by size includes separating isoparaffins from paraffins. 11. The method of claim 9 , wherein separating paraffins by size includes separating linear paraffins from branched paraffins. 12. The method of claim 9 , wherein n-pentane is kinetically separated from isopentane. 13. The method of claim 9 , wherein separating paraffins by size includes separating one or more of linear paraffins and mono-branched paraffins from 2,2,4-trimethylpentane. 14. The method of claim 9 , wherein M III includes one or more of any one of the following trivalent cations of a rare earth element: Ce 3+ , Dy 3+ , Er 3+ , Eu 3+ , Gd 3+ , Ho 3+ , La 3+ , Lu 3+ , Nd 3+ , Pr 3+ , Pm 3+ , Sm 3+ , Sc 3+ , Tb 3+ , Tm 3+ , Yb 3+ , or Y 3+ . 15. The method of claim 9 , wherein X is lithium, sodium, potassium, rubidium, cesium, francium, beryllium, magnesium, calcium, strontium, barium, or radium. 16. The method of claim 9 , wherein paraffins with high cetane numbers are separated from paraffins with low cetane numbers. 17. The method of claim 9 , wherein paraffins with a kinetic diameter of greater than about 4.2 Å to 5.0 Å are separated from paraffins with a smaller kinetic diameter. 18. The method of claim 9 , wherein paraffins with high research octane numbers are separated from paraffins with low research octane numbers. 19. The method of claim 18 , wherein the paraffins with low research octane numbers include one or more of linear paraffins and mono-branched paraffins.
using catalysts, e.g. selective catalysts · CPC title
Hydrocarbons · CPC title
Hydrocarbons · CPC title
Metal organic frameworks (MOF's) · CPC title
by adsorption, e.g. preparative gas chromatography {(solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01)} · CPC title
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