“…For example, the commercial DF-120 membrane with a thickness of 320 μm has proton dialysis coefficient (U H þ ) of only 0.0085 m h À 1 at 25°C and its processing capability for acid recovery from this acidic waste solution is only about 11.3 L m À 2 d À 1 . To date, the various methods have been employed for the modification of dense AEMs [17][18][19][20][21][22][23][24], however, valuable improvement in proton permeability is still difficult.…”