The above objects are achieved by providing a novel process for the production of
hydrogen peroxide, by the non-hazardous direct oxidation of
hydrogen by
oxygen to
hydrogen peroxide, without the formation of an explosive H2 and O2 gas mixture, using a novel tubular hydrophobic composite Pd-membrane catalyst, represented by a formula:Wherein: IPM is an inorganic
porous membrane, permeable to all gases and vapors, in a form of tube having a thickness of at least 0.5 mm and internal
diameter of at least 0.6 cm; Mx Pd1-x is a
metal alloy, permeable only to hydrogen gas, deposited on the inner side of IPM; Pd is a
palladium metal; M is a
metal selected from
copper, silver, gold, noble metals other than
palladium, or a mixture of two or more thereof; x is a
mole fraction of the metal M in the
metal alloy (MxPd1-x) in the range from about 0.03 to about 0.6; (a) is a weight of the
metal alloy per unit area of IPM in the range from about 5.0 g.m-2 to about 500 g.m-2; SOMF is a surface oxidized
thin metal film comprising
palladium which is permeable only to hydrogen, deposited on the
metal alloy (Mx Pd1-x); (b) is a thickness of SOMF in the range from about 0.05 mum to about 5.0 mum; HPM is a
hydrophobic polymer membrane permeable to hydrogen and
oxygen gases and also to vapors of water and
hydrogen peroxide but not to
liquid water or
aqueous solution; and (c) is a weight of the HPM per unit area of SOMF in the range from about 0.2 g.m-2 to about 40 g.m-2.