Solid-state copper(i) sorbents for olefin separations

US2021387134A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2021387134-A1
Application numberUS-201917285524-A
CountryUS
Kind codeA1
Filing dateOct 15, 2019
Priority dateOct 15, 2018
Publication dateDec 16, 2021
Grant date

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Abstract

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Disclosed herein is a process for separating a hydrocarbon feed gas mixture comprising constituents including ethylene to produce a separated ethylene product. The disclosed process employs a solid-state ethylene sorbent and temperature and/or pressure swing adsorption and membrane separation and demonstrates a methodology to reduce the net heat of reaction during the adsorption of ethylene onto an adsorbent.

First claim

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1 . A process comprising: exposing a trinuclear copper(I) pyrazolate complex to a hydrocarbon feed gas mixture comprising one or more alkenes comprising ethylene, propylene, butene, pentene, or isobutylene and one or more alkanes comprising ethane, methane, propane, butane, or pentane, to form a product comprising a dinuclear copper(I)-alkene complex. 2 . (canceled) 3 . (canceled) 4 . (canceled) 5 . (canceled) 6 . The process of claim 1 , wherein the one or more alkenes comprise ethylene, wherein the one or more alkanes comprise ethane, and wherein the formed product comprises a dinuclear copper(I)-ethylene complex. 7 . The process of claim 6 , further comprising a step of separating ethylene from ethane. 8 . The process of claim 6 , wherein the dinuclear copper(I)-ethylene complex is formed by adsorption of ethylene on the trinuclear copper(I) pyrazolate complex. 9 . The process of claim 8 , further comprising a step of desorption of ethylene from the dinuclear copper(I)-ethylene complex at a temperature from about −50° C. to about 150° C. and a pressure from about 0 bar to about 500 bar. 10 . (canceled) 11 . The process of claim 9 , wherein the ethylene desorption forms a regenerated trinuclear copper(I) pyrazolate complex. 12 . The process of claim 1 , wherein the trinuclear copper(I) pyrazolate complex is a [3,4,5-tris(trifluoromethyl)pyrazolyl)Cu] 3 complex ([(3,4,5-(CF 3 ) 3 Pz)Cu] 3 , ([Cu 3 ]). 13 . The process of claim 6 , wherein the dinuclear copper(I)-ethylene complex is a [3,4,5-tris(trifluoromethyl)pyrazolyl)Cu(C 2 H 4 )] 2 ([3,4,5-(CF 3 ) 3 Pz)Cu(C 2 H 4 )] 2 complex, ([Cu 2 .(C 2 H 4 ) 2 ]). 14 . (canceled) 15 . The process of claim 8 , wherein at least a portion of the ethylene adsorption occurs at a ‘step’ pressure of about 2 kPa to about 30 kPa and a temperature from about 20° C. to about 75° C. (from about 293 K to about 348 K). 16 . The process of claim 12 , wherein the step of exposing comprises exposing a solid-state [Cu 3 ] or a dichloromethane solution of [Cu 3 ] to the hydrocarbon feed gas mixture. 17 . (canceled) 18 . The process of claim 11 , wherein the ethylene desorption from dinuclear copper(I)-ethylene complex to regenerate trinuclear copper(I) pyrazolate complex is performed in a solid-state. 19 . The process of claim 13 , wherein the step of exposing results in a reversible solid-state structural transformation [Cu 3 ] to [Cu 2 .(C 2 H 4 ) 2 ]. 20 . (canceled) 21 . The process of claim 12 , wherein an adsorption selectivity of ethylene/ethane on [Cu 3 ] is from about 1:1 to about 136:1 when measured at a temperature of 20° C. and an equilibrium loading at 1 atm or wherein an adsorption selectivity of ethylene/ethane on [Cu 3 ] is from about 1:1 to about 131:1 when measured at a temperature of 70° C. and an equilibrium loading at 1 atm. 22 . (canceled) 23 . The process of claim 12 , wherein the process exhibits a decrease of a heat of adsorption by 50 to 85% when compared to a substantially identical reference process comprising a copper (I) complex that is not [Cu 3 ]. 24 . The process of claim 12 , wherein [Cu 3 ] is formed by: a) reacting copper (I) oxide with a precursor 3,4,5-(CF 3 ) 3 pyrazole (3,4,5-(CF 3 ) 3 PzH) in a solvent-free process to form a product comprising a [3,4,5-tris(trifluoromethyl)pyrazolyl)Cu] 3 complex ([(3,4,5-(CF 3 ) 3 Pz)Cu] 3 , ([Cu 3 ]); b) extracting [Cu 3 ] with a solvent. 25 . (canceled) 26 . The process of claim 24 , further comprising removing the solvent to form a solid-state [Cu 3 ]. 27 . A composition comprising a trinuclear copper(I) pyrazolate complex, wherein the composition is reversibly transformed to a dinuclear copper(I)-alkene complex, when exposed to a hydrocarbon feed gas mixture comprising one or more alkenes comprising ethylene, propylene, butene, pentene, or isobutylene and one or more alkanes comprising ethane, methane, propane, butane, or pentane. 28 . (canceled) 29 . (canceled) 30 . (canceled) 31 . (canceled) 32 . The composition of claim 27 , wherein the trinuclear copper(I) pyrazolate complex comprises a [3,4,5-tris(trifluoromethyl)pyrazolyl)Cu] 3 complex ([(3,4,5-(CF 3 ) 3 Pz)Cu] 3 , ([Cu 3 ]), wherein the composition is reversibly transformed to the dinuclear copper(I)-alkene complex comprising a [3,4,5-tris(trifluoromethyl)pyrazolyl)Cu(C 2 H 4 )] 2 ([3,4,5-(CF 3 ) 3 Pz)Cu(C 2 H 4 )] 2 , ([Cu 2 (C 2 H 4 ) 2 ]) when exposed to a hydrocarbon feed gas mixture comprising ethylene and one or more alkanes comprising ethane. 33 . The composition of claim 32 , wherein [Cu 2 (C 2 H 4 ) 2 ] is formed by an ethylene adsorption on [Cu 3 ]. 34 . The composition of claim 32 , wherein an ethylene desorption transforms [Cu 2 (C 2 H 4 ) 2 ] to [Cu 3 ]. 35 . The composition of claim 32 , wherein the composition exhibits an adsorption selectivity of ethylene/ethane on [Cu 3 ] of from about 1:1 to about 136:1 when measured at a temperature of 20° C. and an equilibrium loading at 1 atm or wherein the composition exhibits an adsorption selectivity of ethylene/ethane on [Cu 3 ] of from about 1:1 to about 131:1 when measured at a temperature of 70° C. and an equilibrium loading at 1 atm. 36 . (canceled) 37 . The composition of claim 32 , wherein the reversible transformation is an endothermic structural rearrangement of [Cu 3 ]. 38 . The composition of claim 32 , wherein the reversible transformation is a solid-state transformation.

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What does patent US2021387134A1 cover?
Disclosed herein is a process for separating a hydrocarbon feed gas mixture comprising constituents including ethylene to produce a separated ethylene product. The disclosed process employs a solid-state ethylene sorbent and temperature and/or pressure swing adsorption and membrane separation and demonstrates a methodology to reduce the net heat of reaction during the adsorption of ethylene ont…
Who is the assignee on this patent?
Univ Texas, Univ Colorado Regents
What technology area does this patent fall under?
Primary CPC classification C07F1/08. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Thu Dec 16 2021 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).