In this study, a novel covalent-assisted seeding method is developed to fabricate well-intergrown ZIF-8 membrane on polyimide (PI) substrate with imidazole-2-carboxaldehyde (ICA) as the covalent agent between ZIF-8 layer and PI substrate.Compared to ethylenediamine-crosslinked PI membrane and ZIF-8/PI membrane synthesized without covalent-assisted seeding method, ZIF-8/PI membrane synthesized with ICA covalent-assisted seeding method shows improved pervaporation performance for isopropanol dehydration. Subsequent surface coating with polydimethylsiloxane or polydopamine is applied to mitigate the grain boundary of ZIF-8/PI membrane, which results in a further performance enhancement. The morphologies and physicochemical properties of the resultant membranes are characterized by scanning electron microscope, attenuated total reflectance-Fourier transform infrared, X-ray diffraction, and water contact angle. The effect of operation temperature on the separation performance is also carried out. This work demonstrates the novel covalent-assisted seeding method for the preparation of ZIF-8 membrane with high-performance, which may hold a great potential for various ZIF membranes separation applications. K E Y W O R D S covalent-assisted seeding, isopropanol dehydration, pervaporation, surface coating, ZIF-8 membrane 1 | INTRODUCTION Zeolitic imidazolate frameworks (ZIFs), as a subclass of metal-organic frameworks (MOFs), have been widely used in the past few decadesfor various applications, including gas adsorption and storage, 1-3 chemical sensors, 4,5 catalysis, 6 drug delivery, 7 and membrane separation, [8][9][10][11][12][13][14][15][16][17][18][19] because of their excellent thermal and chemical stability, high surface area, intrinsic porosity, and molecule-scale pore size. Further, with their tunable pore size and adjustable functionality, ZIF materials are also widely employed for the fabrication of separation membranes. They can be applied either as nanofillers in mixed matrix membranes (MMMs) 8-12 or a continuous selective layer supported by various substrates. [13][14][15][16][17][18][19][20][21] However, the poor filler-polymer interaction and the severe aggregation of ZIF particles limit the improvement of separation performance of the resultant MMMs. [22][23][24][25][26] In recent years, continuous ZIF membranes become another research focus, which are more likely to maximize the advantages of ZIFs and achieve high performance (high permeation and high selectivity) in membrane separation.ZIF membranes can be formed on various supporting materials.Conventionally, a large diversity of inorganic materials, such as porous alumina (Al 2 O 3 ), 13-17 porous zinc oxide (ZnO), 18,19 and stainless-steel nets, 20,21 have been reported as substrates for ZIF membranes because