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A process for generating at least one polyol from a feedstock comprising saccharide is performed in a continuous or batch manner. The process involves, contacting hydrogen, water, and a feedstock comprising saccharide, with a catalyst system to generate an effluent stream comprising at least one pol

A process for generating at least one polyol from a feedstock comprising saccharide is performed in a continuous or batch manner. The process involves, contacting hydrogen, water, and a feedstock comprising saccharide, with a catalyst system to generate an effluent stream comprising at least one polyol and recovering the polyol from the effluent stream. The catalyst system comprises at least one metal component with an oxidation state greater than or equal to 2+.

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1. A process for generating at least one polyol from a feedstock comprising: a) contacting, hydrogen, water, and a feedstock comprising at least one saccharide, with a catalyst system comprising an unsupported component comprising a compound comprising an element selected from the group consisting o

1. A process for generating at least one polyol from a feedstock comprising: a) contacting, hydrogen, water, and a feedstock comprising at least one saccharide, with a catalyst system comprising an unsupported component comprising a compound comprising an element selected from the group consisting of IUPAC Groups 4, 5 and 6 of the Periodic Table and having an oxidation state greater than or equal to 2+ wherein the compound of the unsupported component is in a form other than a carbide, nitride or phosphide, and a supported hydrogenation component selected from the group consisting of IUPAC Groups 8, 9, and 10, of the Periodic Table on a solid catalyst support to generate an effluent stream comprising at least one polyol; andb) recovering the polyol from the effluent stream. 2. The process of claim 1 wherein the process is operated in a mode selected from the group consisting of batch mode operation and continuous mode operation. 3. The process of claim 1 wherein the contacting occurs in a reaction zone comprising at least a first input stream and a second input stream, the first input stream comprising at least flowing feedstock and the second input stream comprising flowing hydrogen. 4. The process of claim 3 wherein the first input stream is pressurized prior to the reaction zone and the second input stream is pressurized and heated prior to the reaction zone. 5. The process of claim 3 wherein the first input stream is pressurized and heated to a temperature below the decomposition temperature of the saccharide in the feedstock prior to the reaction zone and the second input stream is pressurized and heated prior to the reaction zone. 6. The process of claim 3 wherein the first input stream and the second input stream further comprise water. 7. The process of claim 1 wherein the saccharide of the feedstock is selected from the group consisting of monosaccharides, disaccharides, oligosaccharides, polysaccharides, and combinations thereof. 8. The process of claim 1 wherein the feedstock comprising saccharide is selected from a group consisting of edible saccharides, inedible saccharides, waste materials, recycled materials, and combinations thereof. 9. The process of claim 1 wherein the feedstock comprising saccharide is selected from the group consisting of short rotation forestry, industrial wood waste, forest residue, agricultural residue, energy crops, industrial wastewater, municipal wastewater, paper, cardboard, fabrics, pulp derived from biomass, corn starch, sugarcane, grain, sugar beet, glycogen, molecules comprising the molecular unit structure of Cm(H2O)n, and combinations thereof. 10. The process of claim 1 wherein the polyol is selected from the group consisting of ethylene glycol and propylene glycol. 11. The process of claim 1 wherein the effluent stream further comprises at least one co-product selected from the group consisting of alcohols, organic acids, aldehydes, monosaccharides, polysaccharides, phenolic compounds, hydrocarbons, glycerol, depolymerized lignin, and proteins. 12. The process of claim 1 further comprising preparing the feedstock comprising saccharide prior to contacting with the catalyst by a technique selected from the group consisting of sizing, drying, grinding, hot water treatment, steam treatment, hydrolysis, pyrolysis, thermal treatment, chemical treatment, biological treatment, catalytic treatment, and combinations thereof. 13. The process of claim 12 wherein the chemical treatment comprises acid catalyzed hydrolysis or base catalyzed hydrolysis, the catalytic treatments comprise depolymerization, hydrogenation, or both, and wherein the biological treatment comprises enzymatic hydrolysis. 14. The process of claim 1 wherein the hydrogen, water, and feedstock is contacted with the catalyst in a reactor having metallurgy comprising a component selected from the group consisting of titanium, zirconium, stainless steel, carbon steel having hydrogen embrittlement resistant coating, carbon steel having corrosion resistant coating. 15. The process of claim 1 wherein the hydrogen, water, and feedstock is contacted with the catalyst in a system selected from the group consisting of an ebullating catalyst bed system, an immobilized catalyst system having catalyst channels, an augured reaction system, a fluidized bed reaction system, a mechanically mixed reaction system, a slurry reactor system, and combinations thereof. 16. The process of claim 1 wherein the hydrogen, water, and feedstock are contacted with the catalyst system in a slurry reactor system operated at a temperature ranging from about 100° C. to about 350° C. and a hydrogen pressure greater than about 150 psig. 17. The process of claim 1 wherein the hydrogen, water, and feedstock are contacted with the catalyst in a reaction zone operated at conditions sufficient to maintain at least a portion of the water in the liquid phase. 18. The process of claim 1 wherein the hydrogen, water, and feedstock are continuously contacted with the catalyst system in a slurry reactor system operated at a water to feedstock weight ratio ranging from about 1 to about 100, a catalyst to feedstock weight ratio of greater than about 0.005, a pH of less than about 10 and a residence time of greater than 5 minutes. 19. The process of claim 1 wherein the effluent stream further comprises catalyst, said process further comprising separating catalyst from the effluent stream using a technique selected from the group consisting of direct filtration, settling followed by filtration, hydrocyclone, fractionation, centrifugation, the use of flocculants, precipitation, liquid extraction, adsorption, evaporation, and combinations thereof. 20. The process of claim 19 further comprising recycling the separated catalyst to the reactor.