“…The highest activity of TOF = 210 h −1 was exhibited by the RuCl 3 •3H 2 O/TPPTS catalytic system, whereas with the Ru(acac) 3 /TPPTS system the activity was lower to achieve 202 TOF's per hour, and the conversion of LA and selectivity to GVL were 99 and 97 mol%, respectively. Moustani et al (2018) investigated the hydrogenation reaction of LA using RuCl 3 •3H 2 O, Ru(NO)(OAc) 3 , Ru(NO)(NO 3 ) 3 , Ru(acac) 3 , [Ru(NO)] 2 (SO 4 ) 3, and RuO 2 •H 2 O catalyst precursors modified with water-soluble phosphine and especially with nitrogen-containinig ligands such as TPPTS, PTA, bathophenanthrolinedisulfonic acid disodium salt (BPhDS), bathocuproinedisulfonic acid disodium salt (BCDS), 2-aminoethanesulfonic acid (taurine), nitrilotriacetic acid trisodium salt (NTA•Na 3 ), ethylenediaminetetraacetic acid tetrasodium salt (EDTA•Na 4 ), 2,2'-biquinoline-4,4'dicarboxylic acid dipotassium salt (BQC), tris(2-pyridyl)phosphine (T 2 PyP), N,N'-2,2'-bipyridine-4,4'-dicarboxylic acid (BPyDCA), diethylenetriaminepentakis(methylphosphonic acid) (DTPPA), diethylenetriaminepentaacetic acid pentasodium salt (DTPA•Na 5 ) and 3-pyridinesulfonic acid (3-PSA) (Figure 8) in the aqueous monophasic system. The highest activity of TOF = 3,000 h −1 was obtained with RuCl 3 •3H 2 O/BPhDS catalysts at 140 • C, 80 bar H 2 pressure within 1 h and molar ratios of LA/Ru = 3,000 and BPhDS/Ru=1 with addition of 5 ml of aqueous solvent by a ruthenium concentration of 75 ppm and pH value of 2.43 where the conversion of LA was quantitative with essentially quantitative selectivity to GVL of 99.9 mol% and formation of only 0.1 mol % of the 1,4-PDO byproduct.…”