The water pollut ion by heavy meta l ions has become the ser ious t hreat to the huma n healt h,living resources,ecologica l systems and the sustainable developme nt of socia l economy.How to effective ly remo ve the hea vy meta ls in aqueous so lu t ion has been attracted great attent ion b y researchers and t he gover nments around the word.In this work,us ing graphe ne oxide loaded Fe3O4 nanopartic les as carriers,magnet ic graphene oxide gra fted different hydrophobic cha in le ngth a nd end groups dendr imers used for adsorption of hea vy metal ions in aqueous solut io n were fabricated by diver gent method and magnet ic separatio n techno logy.(1)First ly,the hexa met hyle nedia mine(HMD)modified ma gnet ic graphene oxide(HMGO-N H2)was prepared by solvother ma l method,then us ing HMGO-N H2 as carr ier,hexa methyle nedia min and met hyl acrylate(MA)as funct ion mono mers,magnet ic graphene oxide grafted longer hydrophobic chain lengt h low-generat ion hexa methylened ia mine t ype polyamidoa mine dendr imer(HMGO-PAMAM-G1.0)was fabricated by divergent met hod and magnet ic separation technolo gy.The morpholo gy,structure and compos it ion o f the sa mp les were characterized by trans miss ion e lectron microscope(TEM),X-ray diffract ion(X RD),Fourier trans for m infrar ed spectrometer(FT-IR),N2 adsorption/desorption isother m,thermo gravimetr ic analyzer(TG A),vibrating samp le magnetometer(VSM)and X-ray photoelectron spectrometer(XPS).The adsorpt ion propert ies of MGO-PAMAM-G1.0 and HMGO-PAMAM-G1.0 for Pb(II)and Hg(II)in s ingle s ystem were studied by batch experime nts.The adsorption experiment data of MGO-PAMAM-G1.0 and HMGO-PAMAM-G1.0 for Pb(II)and Hg(II)were obtained by us ing k inet ic models and isother m models.The results showed that the superparamagnet ic HMGO-PAMAM-G1.0 was successfully prepared.The specific saturat ion magnet izat io n of HMGO-PAMAM-G1.0 was 25.9 emu·g-1,which can be quick ly separated fro m aqueous solut ion under externa l magnet ic fie ld.Compared w ith MGO-PAMAM-G1.0,HMGO-PAMAM-G1.0 had a lar ger average poresize and a sma ller BET specific sur face area,higher adsorptio n rate and lower adsorption capacit ies for Pb(II)and Hg(II).The adsorptio n processes of MGO-PAMAM-G1.0 and HMGO-PAMAM-G1.0 for Pb(II)and Hg(II)could be described by the pseudo-first-order kinet ic model and Langmuir isother m model.The analys is of XPS indicated that vale nce state of Pb(II)didn’t change,Hg(II)was part ially reduced to Hg(I)in the adsorptio n process.(2)The terminal groups of a series of magnet ic graphene oxide grafted polya midoamine dendrimers(MGO-PAMAM)were mod ified w ith chlorohydrin to fabricate magnet ic graphene oxide grafted hydroxyl-terminated polya midoamine dendr imers(MGO-PAMAM-O H).MGO-PAMAM-O H for the adsorption of Hg(II)in aqueous solut ion was characterized by transmiss ion e lectron microscope(TEM),X-ray diffractio n(XRD),Four ier transfor m infrared spectrometer(FT-IR),ele menta l analys is,ther mogra vimetr ic ana lyzer(TG A),vibrat ing sa mple ma gneto meter(VSM)and X-ray photoelectron spectrometer(XPS).The results s howed that ma gnet ic graphene oxide gra fted 3.0 generatio n hydroxyl-terminated polya midoamine dendr imers(MGO-PAMAM-O H-G3.0)had better adsorpt ion property,and the maximum adsorptio n capacit y was 129.98 mg·g-1.The adsorptio n process of MGO-PAMAM-O H-G3.0 for H g(II)could be better described by the pseudo–first-order kinet ic model and Langmuir isother ma l adsorptio n model,whic h indicated the adsorption was s ingle la yer che mical adsorptio n on homo geneous surface. |