摘要:
ORGANIC AROMATIC NITROGEN CONTAINING COMPOUNDS, SUCH AS P-PHENYLENEDIAMINE OR 4,4''-METHYLENEDIANILINE, CAN BE HYDROGENATED BY ADMIXING THE COMPOUND WITH HYDROGEN AT A HYDROGEN PARTIAL PRESSURE OF AT LEAST 200 P.S.I., A TOTAL PRESSURE OF FROM 200 P.S.I. TO 15,000 P.S.I., A TEMPERATURE IN THE RANGE OF FROM 100*C. TO 300*C., IN THE PRESENCE OF FROM O% TO 200% BY WEIGHT, BASED ON THE WEIGHT OF THE COMPOUND TO BE HYDROGENATED, OF ADDED AMMONIA, AND IN THE PRESENCE OF FROM 0.001% TO 10% BY WEIGHT, BASED ON THE COMPOUND TO BE HYDROGENATED AND CALCULATED AS METALLIC OF A RUTHENIUM CATALYST SUPPORTED ON AN INERT CARRIER, SAID CATALYST BEING ALKALI MODERATED WITH FROM 0.1% TO 15% OF A BASIC METAL COMPOUND CALCULATED AS THE ALKALI METAL.
摘要:
A MIXTURE OF THE STEREOISOMERS OF 1,4-CYLCOHEXANEDIAMINE NOT AT EQUILIBRIUM IS CONVERTED TO A MIXTURE OF STEREOISOMERS APPROACHING THE EQUILIBRIUM RATIO BY HEATING THE MIXTURE OF STEREOISOMERS TO A TEMPERATURE OF FROM 150* TO 300*C. IN THE PRESENCE OF HYDROGEN AT A PRESSURE OF FROM 50 TO 5,500 POUNDS PER SQUARE INCH AND A TOTAL PRESSURE OF FROM 500 TO 15,000 POUNDS PER SQUARE INCH, IN THE PRESENCE OF FROM 0% TO 200% BY WEIGHT, BASED ON THE WEIGHT OF DIAMINE, OF ADDED AMMONIA, AND IN THE PRESENCE OF FROM 0.001% TO 10% BY WEIGHT, BASED ON THE WEIGHT OF DIAMINE AND CALCULATED AS METALLIC RUTHENIUM, OF A RUTHENIUM CATALYST SUPPORTED ON AN INERT CARRIER, SAID CATALYST BEING ALKALI MODERATED WITH FROM 0.05% TO 15% OF A BASIC ALKALI METAL COMPOUND CALCULATED AS THE ALKALI METAL. EITHER ESSENTIALLY PURE TRANS-1,4-CYCLOHEXANEDIAMINE OR ENRICHED CID-1,4CYCLOHEXANEDIAMINE CAN BE RECOVERED.
摘要:
REDUCTIVE AMINATION OF ALDEHYDES IN THE PRESENCE OF A RHODIUM CATALYST IS CONDUCTED AT TEMPERATURES OF FROM 0* TO 125* C. RHODIUM CATALYSTS ARE PARTICULARLY DIRECTIVE TOWARD SECONDARY AMINES.
摘要:
A mixture of the stereoisomers of bicyclohexyl-4,4''-diamine not at equilibrium is converted to a mixture of stereoisomers approaching the equilibrium ratio by heating the mixture of stereoisomers to a temperature of from 150* to 300* C. in the presence of hydrogen at a pressure of from 50 to 5,500 pounds per square inch gage and a total pressure of from 500 to 15,000 pounds per square inch gage, in the presence of from 0 to 200 percent by weight of added ammonia and from 0.001 to 10 percent by weight, calculated as metallic ruthenium, of a ruthenium catalyst supported on an inert carrier, both percentages being based on the weight of a starting material, said catalyst being alkali moderated with from 0.05 to 15 percent of a basic alkali metal compound calculated as the alkali metal. Either essentially pure trans,trans-bicyclohexyl-4,4''-diamine or an enriched mixture of cis,trans- and cis,cis-bicyclohexyl-4,4''-diamine can be recovered.
摘要:
SUPPORTED RUTHENIUM CATALYSTS ARE MODERATED WITH AN ALKALI METAL HYDROXIDE OR ALKOXIDE BY MIXING THE SUPPORTED CATALYST AND THE ALKALI METAL COMPOUND IN THE REACTION MEDIUM OF A HYDROGENATION PROCESS WHICH MAY CONTAIN UP TO 5% OF WATER, AT A TEMPERATURE RANGING FROM ABOUT 30*C TO ABOUT 300*C. THE MODERATED CATALYST IS AN EFFECTIVE HYDROGENATION CATALYST FOR THE HYDROGENATION OF AROMATC AMINES TO THE CORRESPONDING SATURATED CYCLIC AMINES.
摘要:
ORGANIC AROMATIC NITROGEN CONTAINING COMPOUNDS, SUCH AS P-PHENYLENEDIAMINE OR 4,4''-METHYLENEDIANILINE, CAN BE HYDROGENATED BY ADMIXING THE COMPOUNDS WITH HYDROGEN AT A HYDROGEN PARTIAL PRESSURE OF AT LEAST 200 P.S.I., A TOTAL PRESSURE OF FROM 200 P.S.I. TO 15,000 P.S.I., A TEMPERATURE IN THE RANGE OF FROM 100*C. TO 300*C. IN THE PRESENCE OF FROM 0% TO 200% BY WEIGHT, BASED ON THE WEIGHT OF THE COMPOUND TO BE HYDROGENATED, OF ADDED AMMONIA, AND IN THE PRESENCE OF FROM 0.001% TO 10% BY WEIGHT, BASED ON THE COMPOUND TO BE HYDROGENATED AND CALCULATED AS METALLIC RUTHENIUM, OF A RUTHENIUM CATALYST SUPPORTED ON AN INERT CARRIER SELECTED FROM THE GROUP CONSISTING OF CALCIUM CARBONATE, RARE EARTH OXIDES, RARE EARTH CARBONATES, MIXED RARE EARTH OXIDE-CARBONATES, AND MIXTURES THEREOF.