2005
DOI: 10.1021/ie0488546
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Absorption Equilibrium and Kinetics for Ethylene−Ethane Separation with a Novel Solvent

Abstract: A novel solvent system consisting of CuCl/aniline/n-methyl pyrrolidone was evaluated for the reactive absorption of ethylene. Equilibrium olefin loadings significantly exceeded physical solubility values. The equilibrium ethylene-ethane selectivity was a strong function of the gas phase total pressure. Kinetic behavior was accurately described by an instantaneous reversible mechanism. The solvent exhibited acceptable chemical stability during the experimental tests.

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Cited by 49 publications
(39 citation statements)
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“…These results indicate that Cu(I)Y-V has a high Cu(I) content than Cu(I)Y-A. 40,41 Great attention has been given to the separation of propylene/propane through adsorption, since this process can be carried out under mild conditions. 2.…”
Section: Resultsmentioning
confidence: 96%
“…These results indicate that Cu(I)Y-V has a high Cu(I) content than Cu(I)Y-A. 40,41 Great attention has been given to the separation of propylene/propane through adsorption, since this process can be carried out under mild conditions. 2.…”
Section: Resultsmentioning
confidence: 96%
“…Reine also performed kinetic studies on the CuCl, aniline, and DMF system. 3 These experiments indicated a 1:1 Cu(I) to ethylene ratio in the metal-olefin complexes and a first-order reaction, as shown in Eq. 1.…”
Section: Background and Theory Previous Work On Cucl-aniline-nmp Systemmentioning
confidence: 85%
“…1,3,4 A combination of CuCl, aniline, and N-methylpyrrolidone (NMP) exhibited optimal solution characteristics, including low cost, high ethylene capacity, low volatility, and high stability. However a lack of basic understanding regarding the structure of the Cu(I)-ethylene-aniline complex impedes the development of reactive absorption systems.…”
Section: Introductionmentioning
confidence: 99%
“…Conventional olefin/paraffin separation technologies are based on cryogenic distillation process in columns with 150-200 trays operating at temperatures between 233 and 183 K and pressures ranging from 16 to 20 bar which lead to high capital investment, operational cost and also negative environmental impact [1][2][3]. Therefore, it is critical to develop innovative and cost-effective technologies able to separate these streams, overcoming the drawbacks associated to conventional systems.…”
Section: Introductionmentioning
confidence: 99%