Method of purifying polluted water

Claim 2

In the liquid phase catalytic oxidation of organically polluted water, containing no more than about 1 part of alkali metal ions per million parts of polluted water, to reduce the total oxygen demand of said polluted water by contacting said polluted water with an oxygen-containing gas and a catalyst effective to promote such liquid phase oxidation comprising zinc aluminate promoted with at least one metal active for initiating oxidative reactions, the method of increasing the catalyst life comprising adding a sufficient amount of alkali metal ion to the organically polluted water prior to the catalytic oxidation to increase the throughput that can occur before the pH breakthrough occurs.

Claim 3

The method according to claim 1 wherein the amount of alkali metal ion employed is continuously reduced as the TOD of the treated water approaches a chosen maximum.

Claim 4

The method according to claim 1 wherein the alkali metal ion is added in the form of an alkali metal hydroxide or an alkali metal salt of weak acid.

Claim 5

The method according to claim 3 wherein the alkali metal is sodium.

Claim 6

The method according to claim 4 wherein the alkali metal concentration of the polluted water to be oxidized is adjusted to be within the range of about 10 to about 300 parts per million parts of the polluted water.

Claim 7

The method according to claim 4 wherein the alkali metal concentration is in the range of about 30 to about 35 parts per million parts of the polluted water.

Claim 8

The method according to claim 6 wherein the pH of the polluted water prior to the addition of the alkali metal ion is less than about 4.

Claim 9

The method according to claim 7 wherein the TOD of the unpurified polluted water is about 2200 mg/liter or less.

Claim 10

The method according to claim 4 wherein the alkali metal ion concentration of the polluted stream is such that the TOD prior to the pH breakthrough is no greater than the maximum allowable value.

Claim 11

The method according to claim 1 wherein the promoting metal is copper, manganese, nickel, cobalt, bismuth, platinum, palladium, rhenium, iridium, lanthanum, cerium, or combinations of those metals.

Claim 12

The method according to claim 1 wherein the catalyst is zinc aluminate promoted with copper, manganese, and lanthanum.

Claim 13

A method according to claim 11 wherein the concentration of promoter metals on the zinc aluminate is in the range of 0.05 to 20 weight percent based on the weight of the zinc aluminate, the temperature of the oxidation is in the range of about 50° C. to about 350° C., the molar ratio of polluted water to oxygen is in the range of 10:1 to 200:1, and the alkali metal concentration of the polluted water is adjusted to be within the range of about 10 to about 300 parts per million parts of the polluted water.

Claim 14

The method according to claim 12 wherein the organically polluted water is the waste aqueous effluent from a hydrocarbon oxidative dehydrogenation process and said organically polluted water prior to the addition of any alkali metal ion is about 4 pH or less and the TOD of the unpurified polluted water is about 2200 mg/liter or less.

Claim 15

In a process for the purification of an aqueous stream, containing dissolved and/or suspended oxidizable organic impurities and no more than about 1 part of alkali metal per million parts of the aqueous stream, to reduce the total oxygen demand of said aqueous stream by contacting said aqueous stream containing oxidizable organic impurities and an oxygen-containing gas with a catalyst consisting essentially of zinc aluminate promoted with 0.05 to 20 weight percent of (1) at least two different metals active for initiating oxidative reactions selected from the group consisting of the metals of the Groups IIIB, IVB, VB, VIB, VIIB, VIII, IB, and VA of the Periodic Table and (2) a rare earth metal under liquid phase oxidation conditions including a temperature in the range of 350° to 550° F. and a molar ratio of water to oxygen in the range of 10:1 to 200:1 to convert said organic impurities to innocuous materials so that said aqueous stream which has been substantially freed of said organic impurities can be safely discarded or reused; the method of increasing catalyst life comprising adjusting the alkali metal concentration of the aqueous stream to be purified to within the range of about 10 to about 300 ppm.

Claim 16

In a process for the purification of an aqueous stream, containing dissolved and/or suspended oxidizable organic impurities and no more than about 1 part of alkali metal per million parts of the aqueous stream, to reduce the total oxygen demand of said aqueous stream by contacting said aqueous stream containing oxidizable organic impurities and an oxygen-containing gas with a catalyst consisting essentially of zinc aluminate promoted with 0.05 to 20 weight percent of (1) at least two different metals active for initiating oxidative reactions selected from the group consisting of the metals of the Groups IIIB, IVB, VB, VIB, VIIB, VIII, IB, and VA of the Periodic Table and (2) a rare earth metal under liquid phase oxidation conditions including a temperature in the range of 350° to 550° F. and a molar ratio of water to oxygen in the range of 10:1 to 200:1 to convert said organic impurities to innocuous materials so that said aqueous stream which has been substantially freed of said organic impurities can be safely discarded or reused; the method of increasing catalyst life comprising adjusting the alkali metal concentration of the aqueous stream to be purified to within the range of about 10 to about 300 ppm.

Claim 17

The method according to claim 14 wherein the alkali metal ion is added in the form of an alkali metal hydroxide or an alkali metal salt of weak acid.

Claim 18

The method according to claim 15 wherein the alkali metal is sodium.

Claim 19

The method according to claim 16 wherein the alkali metal concentration is adjusted to within the range of about 20 to about 70 parts per million parts of the polluted water.

Claim 20

The method according to claim 16 wherein the alkali metal concentration is in the range of about 30 to about 35 parts per million parts of the polluted water.

Claim 21

The method according to claim 18 wherein the pH of the polluted water prior to the addition of the alkali metal ion is less than about 4.

Claim 22

The method according to claim 19 wherein the TOD of the umpurified polluted water is about 2200 mg/liter or less.

Claim 23

The method according to claim 15 wherein the amount of alkali metal ion employed is continuously reduced as the TOD of the treated water approaches a chosen maximum.

Claim 24

In a process for the purification of an aqueous stream, containing dissolved and/or suspended oxidizable organic impurities and no more than about 1 part of alkali metal per million parts of the aqueous stream, to reduce the total oxygen demand of said aqueous stream by contacting said aqueous stream containing oxidizable organic impurities and an oxygen-containing gas with a catalyst consisting essentially of zinc aluminate promoted with 0.05 to 20 weight percent of (1) at least two different metals active for initiating oxidative reactions selected from the group consisting of the metals of the Groups IIIB, IVB, VB, VIB, VIIB, VIII, IB, and VA of the Periodic Table and (2) a rare earth metal under liquid phase oxidation conditions including a temperature in the range of 350° to 550° F. and a molar ratio of water to oxygen in the range of 10:1 to 200:1 to convert said organic impurities to innocuous materials so that said aqueous stream which has been substantially freed of said organic impurities can be safely discarded or reused; the method of increasing catalyst life comprising adding a sufficient amount of alkali metal ion to the aqueous stream prior to the catalytic oxidation thereof to increase the throughput that can occur before the pH breakthrough occurs.

Claim 25

In a process for the purification of an aqueous stream, containing dissolved and/or suspended oxidizable organic impurities and no more than about 1 part of alkali metal per million parts of the aqueous stream, to reduce the total oxygen demand of said aqueous stream by contacting said aqueous stream containing oxidizable organic impurities and an oxygen-containing gas with a catalyst consisting essentially of zinc aluminate promoted with 0.05 to 20 weight percent of (1) at least two different metals active for initiating oxidative reactions selected from the group consisting of the metals of the Groups IIIB, IVB, VB, VIB, VIIB, VIII, IB, and VA of the Periodic Table and (2) a rare earth metal under liquid phase oxidation conditions including a temperature in the range of 350° to 550° F. and a molar ratio of water to oxygen in the range of 10:1 to 200:1 to convert said organic impurities to innocuous materials so that said aqueous stream which has been substantially freed of said organic impurities can be safely discarded or reused; the method of increasing catalyst life comprising adding a sufficient amount of alkali metal ion to the aqueous stream prior to the catalytic oxidation thereof to increase the throughput that can occur before the pH breakthrough occurs.