Catalytic hydrogenation solvents

Table III shows the results of operating the SRT unit in the hydrogen donor mode (catalytically hydrogenated solvent) with and without the addition of Light SRC to the distillate solvent Batch I solvent was used in Run 9 A blend of Batch VI solvent and Light SRC, 70/30 weight ratio, were catalytically hydrogenated as the feed to Runs 1 and 3 The hydrogen donor capability of the solvents were measured by the Equilibrium microautoclave tests These bench-scale SRT results are rather extraordinary in respect to increased distillate yields and improvement in unit operability with addition of Light SRC In Table III the integrated yields refer to the combination of liquefaction, CSD, and catalytic hydrogenation of the solvent ...

Schematically, the polymerization of NBR and the subsequent formation of HNBR by catalytic hydrogenation of NBR are shown in Figures 3.3 and 3.4. It is important to understand Figures 3.3 and 3.4 to understand the cost differential between NBR and HNBR. For example, a medium Acrylonitrile, ACN, medium Mooney viscosity NBR material, typically 33 mole% ACN in the polymer and with a Mooney viscosity of 50 (MLl - -4 at 100°C), may cost roughly 1.00 per pound. Because of the additional steps involved in re-dissolving, catalytic hydrogenation, solvent stripping, and drying, the resulting HNBR polymer can cost in the range of 12.00 to 16.00 per pound. This differential in cost is more easily understood using...

Obtained by the catalytic hydrogenation of naphthalene. Owing to the presence of one aromatic ring it can be nitrated and sulphon-ated. It is non-toxic and is used as a solvent for fats, oils and resins. 

The solvent used m catalytic hydrogenation is chosen for its ability to dissolve the alkene and is typically ethanol hexane or acetic acid The metal catalysts are insoluble m these solvents (or indeed m any solvent) Two phases the solution and the metal are present and the reaction takes place at the interface between them Reactions involving a substance m one phase with a different substance m a second phase are called het erogeneous reactions... 

Carboxylic acids are exceedingly difficult to reduce Acetic acid for example is often used as a solvent in catalytic hydrogenations because it is inert under the reaction con ditions A very powerful reducing agent is required to convert a carboxylic acid to a pri mary alcohol Lithium aluminum hydride is that reducing agent... 

The carbonyl group of carbohydrates can be reduced to an alcohol function Typi cal procedures include catalytic hydrogenation and sodium borohydnde reduction Lithium aluminum hydride is not suitable because it is not compatible with the solvents (water alcohols) that are required to dissolve carbohydrates The products of carbohydrate reduc tion are called alditols Because these alditols lack a carbonyl group they are of course incapable of forming cyclic hemiacetals and exist exclusively m noncyclic forms... 

DIBK can be produced by the hydrogenation of phorone which, in turn, is produced by the acid-catalyzed aldol condensation of acetone. It is also a by-product in the manufacture of methyl isobutyl ketone. Diisobutyl ketone ( 1.37/kg, October 1994) is produced in the United States by Union Carbide (Institute, West Virginia) and Eastman (Kingsport, Teimessee) (47), and is mainly used as a coating solvent. Catalytic hydrogenation of diisobutyl ketone produces the alcohol 2,6-dimethyl-4-heptanol [108-82-7]. 

An improved version of the amine hydrolysis process involves catalytic hydrogenation of 1,3,5-triaitrobenzene or 2,4,6-triaitrobenzoic acid in acetone solvent (138). Acid hydrolysis of 2,4,6-triaminobenzoic acid has been improved by addition of copper catalyst and gives phlorogluciaol in 80% yield (139). 

Dinitrotoluenes can be catalytically hydrogenated to toluenediamines under a wide variety of temperatures, pressures, and solvents the catalyst can be supported noble metal, eg, Pd/C or nickel, either supported or Raney type. The reduction requires six moles of hydrogen per mole of DNT and produces four moles of water. 

Catalytic hydrogenations can be carried out ia the vapor phase or ia the Hquid phase, either with or without the use of a solvent. The vapor phase reaction is limited to compounds which are thermally stable and relatively volatile. High boiling compounds and those which are thermally unstable must be hydrogenated ia the Hquid phase. 

The Zinin reduction is also usehil for the reduction of aromatic nitro compounds to amines in the laboratory. It requires no special equipment, as is the case with catalytic hydrogenations, and is milder than reductions with iron and acid. Usually ammonium or alkah sulfides, hydrosulftdes or polysulftdes are used as the reactant with methanol or ethanol as the solvent. 

Cyclohexanol [108-93-0] is a colorless, viscous liquid with a camphoraceous odor. It is used chiefly as a chemical iatermediate, a stabilizer, and a homogenizer for various soap detergent emulsions, and as a solvent for lacquers and varnishes. Cyclohexanol was first prepared by the treatment of 4-iodocyclohexanol with ziac dust ia glacial acetic acid, and later by the catalytic hydrogenation of phenol at elevated temperatures and pressures. 

The industrial processes used for reduction are catalytic hydrogenation, iron reduction (aqueous neutral or acidic, or solvent), and sulfide reduction. 

Solvents are often used in catalytic hydrogenation (< 7). Solvents may be one of the best means available for markedly altering the selectivity, a fact not sufficiently appreciated. Solvents also help to moderate the heat of hydroge nation, to aid in catalyst handling and recovery, and to permit the use of solid substrates. A convenient solvent may be the product itself or the solvent used in a prior or subsequent step. 

There are several sources of potential danger in catalytic hydrogenations these are failure of equipment because of excessive pressures, solvent fires, explosions and fires from mixtures of hydrogen in air, and, with finely divided carbon supports, dust explosions. None of these should cause concern, for all may be avoided easily. 

The ester 3 (R1 = H, R2 = (CH2)3NMe2 23 g. 67 mmol), obtained by catalytic hydrogenation of the corresponding nitro compound, was heated in refluxing xylene (700 mL) for 15 h. The solvent was removed under reduced pressure and the residue was dissolved in 1 M HOAc and charcoal was added. The filtered solution was made alkaline with coned NH3 and the resulting precipitate was extracted with CHC1V The extract was washed with H20, dried and evaporated in vacuo, leaving the product yield 9.25 g (47%) mp 151-152 C. 

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