1979
DOI: 10.1007/bf00723875
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Recovery and utilization of by-product acetylene from olefin production

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Cited by 6 publications
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“…However, the C 2 H 2 /C 2 H 4 separation is a long-standing challenge because they have similar kinetic diameters (C 2 H 2 : 3.3 Å vs. C 2 H 4 : 4.1 Å) and similar physicochemical properties. 4 Current strategies for the separation of C 2 H 2 from C 2 H 4 in industrial processes are mainly cryogenic distillation, catalytic hydrogenation of C 2 H 2 to C 2 H 4 , and solvent extraction. 5 These processes are either energy-/cost-intensive or environmentally unfriendly.…”
Section: Introductionmentioning
confidence: 99%
“…However, the C 2 H 2 /C 2 H 4 separation is a long-standing challenge because they have similar kinetic diameters (C 2 H 2 : 3.3 Å vs. C 2 H 4 : 4.1 Å) and similar physicochemical properties. 4 Current strategies for the separation of C 2 H 2 from C 2 H 4 in industrial processes are mainly cryogenic distillation, catalytic hydrogenation of C 2 H 2 to C 2 H 4 , and solvent extraction. 5 These processes are either energy-/cost-intensive or environmentally unfriendly.…”
Section: Introductionmentioning
confidence: 99%
“…5 Presently, the separation of acetylenes from olefins is accomplished by costly solvent extraction processes using organic solvents such as EG (ethylene glycol), DMF (N,N 0 -dimethylformamide) and NMP (N-methylpyrrolidinone). 6,7 However, this process is disadvantageous in terms of technical and economical aspects, particularly due to the low selectivities of acetylenes over olefins and also to the significant loss of solvent after multiple operations.…”
Section: Introductionmentioning
confidence: 99%