2015
DOI: 10.1039/c4sc03128h
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Dehydrogenation, disproportionation and transfer hydrogenation reactions of formic acid catalyzed by molybdenum hydride compounds

Abstract: Cyclopentadienyl molybdenum hydride compounds are catalysts for dehydrogenation, disproportionation and transfer hydrogenation reactions of formic acid, in which the latter provides a means to reduce aldehydes and ketones.

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Cited by 81 publications
(72 citation statements)
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“…595 The results obtained with these two molybdenum catalysts should trigger the further development of molybdenumcatalyzed TH. Rhenium complexes have recently been reported as catalysts in TH of CO, CC, and CN bonds (Scheme 79) since the pioneering work in this field by Toste and Kwong et al 602,603 Togni's group 597 synthesized new air-and moisturestable rhenium complexes such as 208 that have chiral ferrocenyldiphosphine ligands of the Josiphos family and used them as catalysts in the ATH of ketones using 2-PrOH as reducing reagent and substoichiometric amounts of triethylamine as base.…”
Section: Osmium-based Catalystsmentioning
confidence: 97%
“…595 The results obtained with these two molybdenum catalysts should trigger the further development of molybdenumcatalyzed TH. Rhenium complexes have recently been reported as catalysts in TH of CO, CC, and CN bonds (Scheme 79) since the pioneering work in this field by Toste and Kwong et al 602,603 Togni's group 597 synthesized new air-and moisturestable rhenium complexes such as 208 that have chiral ferrocenyldiphosphine ligands of the Josiphos family and used them as catalysts in the ATH of ketones using 2-PrOH as reducing reagent and substoichiometric amounts of triethylamine as base.…”
Section: Osmium-based Catalystsmentioning
confidence: 97%
“…Secondly, synthesis gas is converted to methanol using Cu‐based heterogeneous catalysts at typically 220–260 °C and 70–80 bar . The next step is the carboxylation of methanol with additional CO to generate the intermediate formic acid methyl ester, which is typically at 80 °C and 45 bar using a Na methoxide catalyst . The final step is the subsequent hydrolysis of the ester using an excess of water at typically 100–140 °C and 1 bar in order to produce FA and methanol, whereby the latter can be recycled back into the former step and initiate a new reaction sequence …”
Section: Introductionmentioning
confidence: 99%
“…[23][24][25] Then ext step is the carboxylationo fm ethanol with additional CO to generatet he intermediate formic acid methyl ester, which is typically at 80 8Cand 45 bar using aNamethoxide catalyst. [26] Thef inal step is the subsequent hydrolysis of the ester using an excess of water at typically 100-140 8Ca nd 1bar in order to produce FA and methanol, wherebythe latter can be recycled backi nto the former step and initiatean ew reaction sequence. [25,27] In the last years,e lectrochemical reduction of carbon dioxide was suggested asa na lternative way to produce FA.…”
Section: Introductionmentioning
confidence: 99%
“…[3,4] In addition, both FA and MeOH may be utilizeda se asy-to-handle H 2 storagem edia. [15][16][17] To date, the bestr esultsf or the FA disproportionation reactionr eport aM eOH yield of 50 %( with 50 %c ompeting dehydrogenation) in THF at 150 8C, in the presence of aruthenium-phosphine catalyst andamethanesulfonic acid additive. [6] In recent years, an umber of groups has investigated the conversion of CO 2 derivatives or CO 2 to methanoli nt he presence of homogeneous catalysts.…”
mentioning
confidence: 99%
“…[7][8][9][10][11][12][13][14] Commonf eatures of these works wereh igh temperatures (over 100 8C), the employment of organic solvents, and, in certain cases, low selectivities. [15][16][17] To date, the bestr esultsf or the FA disproportionation reactionr eport aM eOH yield of 50 %( with 50 %c ompeting dehydrogenation) in THF at 150 8C, in the presence of aruthenium-phosphine catalyst andamethanesulfonic acid additive. (1)] and disproportionation of the latter into methanol [Eq.…”
mentioning
confidence: 99%