Steam reforming process

Claim 1

The method of steam reforming a charge hydrocarbon which comprises passing mixture of steam and charge hydrocarbon into contact with a steam reforming catalyst containing oxide of nickel and oxide of chromium at steam reforming reaction conditions including temperature of 800°-1100° F. and pressure of 0-100 psig for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge hydrocarbon to product hydrogen, decreases during the reaction period; interrupting said reaction period when the activity of said catalyst has decreased, said interrupting being effected by decreasing the flow of said charge hydrocarbon; contacting said catalyst of decreased activity with steam during a regeneration period at regenerating conditions, including temperature of 800°-1100° F. and pressure of 0-100 psig for 90-540 seconds, as the activity of said catalyst increases, thereby forming regenerated catalyst; and recovering product hydrogen.

Claim 2

The method of steam reforming a charge hydrocarbon which comprises passing mixture of steam and charge hydrocarbon into contact with a steam reforming catalyst containing oxide of nickel and oxide of chromium at steam reforming reaction conditions including temperature of 800°-1100° F. and pressure of 0-100 psig for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge hydrocarbon to product hydrogen, decreases during the reaction period; interrupting said reaction period when the activity of said catalyst has decreased, said interrupting being effected by decreasing the flow of said charge hydrocarbon; contacting said catalyst of decreased activity with steam during a regeneration period at regenerating conditions, including temperature of 800°-1100° F. and pressure of 0-100 psig for 90-540 seconds, as the activity of said catalyst increases, thereby forming regenerated catalyst; and recovering product hydrogen.

Claim 8

The method of steam reforming a charge hydrocarbon which comprises passing a mixture of steam and charge hydrocarbon into contact with a steam reforming catalyst at steam reforming reaction conditions including temperature of 800°-1100° F. and pressure of 0-100 psig for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge hydrocarbon to product hydrogen, decreases to less than about 90% of the initial activity during a reaction period, interrupting said reaction period when the activity of said catalyst has decreased to less than about 90%, said interrupting being effected by decreasing the flow of said charge hydrocarbon; contacting said catalyst of decreased activity which steam during a regeneration period at regenerating conditions, including temperature of 800°-1100° and pressure of 0-100 psig for 90-540 seconds, as the activity of said catalyst increases to at least about 75% of its initial activity thereby forming regenerated catalyst; and recovering product hydrogen.

Claim 9

The method of steam reforming a charge hydrocarbon which comprises passing a mixture of steam and charge hydrocarbon into contact with a steam reforming catalyst at steam reforming reaction conditions including temperature of 800°-1100° F. and pressure of 0-100 psig for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge hydrocarbon to product hydrogen, decreases to less than about 90% of the initial activity during a reaction period, interrupting said reaction period when the activity of said catalyst has decreased to less than about 90%, said interrupting being effected by decreasing the flow of said charge hydrocarbon; contacting said catalyst of decreased activity which steam during a regeneration period at regenerating conditions, including temperature of 800°-1100° and pressure of 0-100 psig for 90-540 seconds, as the activity of said catalyst increases to at least about 75% of its initial activity thereby forming regenerated catalyst; and recovering product hydrogen.

Claim 16

The method of steam reforming charge toluene which comprises passing a mixture of steam and toluene into contact with a steam reforming catalyst at steam reforming conditions including temperature of 800°-1100° F. for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge toluene to product hydrogen, decreases during a reaction period; interrupting said reaction period when the activity of said catalyst has decreased, said interrupting being effected by decreasing the flow of said charge hydrocarbon; contacting said catalyst of decreased activity with steam during a regeneration period at regenerating conditions including temperature of 800°-1100° F., as the activity of said catalyst increases thereby forming regenerated catalyst; and recovering product gas containing hydrogen.

Claim 17

The method of steam reforming charge toluene which comprises passing a mixture of steam and toluene into contact with a steam reforming catalyst at steam reforming conditions including temperature of 800°-1100° F. for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge toluene to product hydrogen, decreases during a reaction period; interrupting said reaction period when the activity of said catalyst has decreased, said interrupting being effected by decreasing the flow of said charge hydrocarbon; contacting said catalyst of decreased activity with steam during a regeneration period at regenerating conditions including temperature of 800°-1100° F., as the activity of said catalyst increases thereby forming regenerated catalyst; and recovering product gas containing hydrogen.

Claim 19

The method of steam reforming charge stream containing paraffin hydrocarbons which comprises passing a mixture of steam and said charge stream into contact with a steam reforming catalyst at steam reforming conditions including temperatures of 800°-1100° F., pressure of 0-100 psig, and steam to hydrocarbon mole ratio of 25-125:1 for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge hydrocarbon to product hydrogen decreases to 50-90% of its initial activity during a reaction period; interrupting said reaction period when the activity of said catalyst has decreased to a point at which the activity is less than 90% of the initial activity, said interrupting being effected by decreasing the flow of said charge hydrocarbon; decreasing the flow of charge hydrocarbon to 0%-50% of that of the reaction period during a regenerating period; contacting said catalyst of decreased activity with steam at regenerating conditions including temperature of 800°-1100° F., pressure of 0-100 psig, and a weight hourly space velocity WHSV of 0.1-2 for 90-540 seconds as the activity of said catalyst increases to 80%-100% of its initial activity thereby forming regenerated catalyst; and recovering product gas containing hydrogen.

Claim 20

The method of steam reforming charge stream containing paraffin hydrocarbons which comprises passing a mixture of steam and said charge stream into contact with a steam reforming catalyst at steam reforming conditions including temperatures of 800°-1100° F., pressure of 0-100 psig, and steam to hydrocarbon mole ratio of 25-125:1 for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge hydrocarbon to product hydrogen decreases to 50-90% of its initial activity during a reaction period; interrupting said reaction period when the activity of said catalyst has decreased to a point at which the activity is less than 90% of the initial activity, said interrupting being effected by decreasing the flow of said charge hydrocarbon; decreasing the flow of charge hydrocarbon to 0%-50% of that of the reaction period during a regenerating period; contacting said catalyst of decreased activity with steam at regenerating conditions including temperature of 800°-1100° F., pressure of 0-100 psig, and a weight hourly space velocity WHSV of 0.1-2 for 90-540 seconds as the activity of said catalyst increases to 80%-100% of its initial activity thereby forming regenerated catalyst; and recovering product gas containing hydrogen.

Claim 21

The method of steam reforming charge hydrocarbon containing C 9 -C 11 hydrocarbon components which comprises passing a mixture of steam and charge into contact with a steam reforming catalyst at steam reforming conditions including temperature of 800°-1100° F. for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge hydrocarbon to product hydrogen decreases to less than about 90% of the initial activity during a reaction period; interrupting said reaction period when the activity of said catalyst has decreased to less than about 90%, said interrupting being effected by decreasing the flow of said charge hydrocarbon; contacting said catalyst of decreased activity with steam during a regeneration period at regenerating conditions including temperature of 800°-1100° F., as the activity of said catalyst increases to at least about 75% of its initial activity thereby forming regenerated catalyst; and recovering product gas containing hydrogen.

Claim 22

The method of steam reforming charge hydrocarbon containing C 9 -C 11 hydrocarbon components which comprises passing a mixture of steam and charge into contact with a steam reforming catalyst at steam reforming conditions including temperature of 800°-1100° F. for 30-180 seconds during which time the activity of the steam reforming catalyst, as measured by the mole percent conversion of charge hydrocarbon to product hydrogen decreases to less than about 90% of the initial activity during a reaction period; interrupting said reaction period when the activity of said catalyst has decreased to less than about 90%, said interrupting being effected by decreasing the flow of said charge hydrocarbon; contacting said catalyst of decreased activity with steam during a regeneration period at regenerating conditions including temperature of 800°-1100° F., as the activity of said catalyst increases to at least about 75% of its initial activity thereby forming regenerated catalyst; and recovering product gas containing hydrogen.