sions by 2050. The industrial separation processes are responsible for approximately half the energy consumption of the U.S. industry, which corresponds to 10-15% of the total U.S. energy consumption. [1,2] In a similar vein, the conventionally used high pressure cryogenic distillation processes accounts for 30% of the total energy consumption for the production of ethylene in petrochemical industry. [3] Membrane separation technology is an attractive alternative to the aforementioned energy-intensive separation process owing to its small footprint and high energy efficiency. [4,5] Despite extensive efforts, ethylene/ethane (C 2 H 4 /C 2 H 6 ) separation remains challenging owing to marginal difference in both their size and condensability. [6] To date, various materials have been investigated for high performance C 2 H 4 / C 2 H 6 separation with varying degrees of success. [7][8][9][10][11][12][13] For instance, facilitated transport membranes exhibit outstanding separation performance owing to carrier mediated-transport, but they suffer from carrier instability when exposed to light or gases such as hydrogen, hydrogen sulfide, or acetylene. [14] Carbon molecular sieve membranes derived from pyrolysis of polymer precursors present a unique opportunity for the tuning of pore structure for optimal C 2 H 4 /C 2 H 6 separation. [15] However, physical aging and chemical or physical adsorption of oxygen, water, or organics have been major hurdles to achieving attractive separation performance. [16][17][18] As an alternative, composite membranes prepared by embedding porous fillers into polymer matrix, referred to as mixed matrix membranes (MMM), have garnered significant attention owing to the easy processability of polymers and superior separation performance of fillers.Metal organic frameworks (MOFs) have been identified as promising fillers for C 2 H 4 /C 2 H 6 separation owing to their enhanced C 2 H 4 adsorption via π-complexation with open metal sites (OMS) of specific metals (Cu(I), Ag(I), or Ni). [19,20] A series of MOFs, such as M-MOF-74 (M = Co, Ni), Cu 3 BTC 2, and MIL-101 (Cr) have been reported to be promising for C 2 H 4 /C 2 H 6 separation. Ploegmakers et al. developed a P84 polymer matrix containing 20 wt% of Cu 3 BTC 2 , which exhibited a 73% increase in C 2 H 4 /C 2 H 6 selectivity while maintaining C 2 H 4 permeability remained constant. [8] Moreover, Bachman et al. reported that the 6FDA-DAM/M-MOF-74 (M = Ni) MMM exhibited significant Herein, a new approach for the in situ synthesis of zeolitic imidazolate framework (ZIF) nanoparticles with triple ligands, referred to as Sogang ZIF-8 (SZIF-8), is reported for enhanced C 2 H 4 /C 2 H 6 kinetic separation. SZIF-8 consists of tetrahedral zinc metals coordinated with tri-butyl amine (TBA), 2,4-dimethylimidazole (DIm), and 2-methylimidazole (MIm). SZIF-8(x) with different DIm contents in x (up to 23.2 mol%) are synthesized in situ because TBA preferably deprotonates DIm ligands due to the much lower pK a of DIm over MIm, allowing for the Zn-DIm coordin...