“…[15] The most common strategies of obtaining TPP from recycling of TPPO are by using chemical reductants like silyl hydrides, [16] aluminium hydrides, [17] boranes, [18,19] and so on. [15,[20][21][22][23][24][25][26][27][28][29][30][31][32][33][34][35][36][37] The bond dissociation energy of the PÀ Cl bond (H 2 PÀ Cl, 315.1 kJ/mol) is less than that of the PÀ O bond (H 2 PÀ OH, 359.7 kJ/mol). Therefore, chlorination of TPPO by oxalyl chloride and/or phosgene followed by reduction by hydrogenation at high pressure in presence of metal catalysts (Pt, Rh, Pd, Na, Fe, Al) remained an alternative approach.…”