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A method of oxidizing an organic material in an oxidizer includes forming a mixture of the organic material with water and a fluid including oxygen under conditions near supercritical pressure. At the inlet of the oxidizer, the mixture is caused to undergo reaction under supercritical conditions for

A method of oxidizing an organic material in an oxidizer includes forming a mixture of the organic material with water and a fluid including oxygen under conditions near supercritical pressure. At the inlet of the oxidizer, the mixture is caused to undergo reaction under supercritical conditions for water, characterized by a temperature of at least about 400° C. and a pressure of at least about 220 atmospheres in the oxidizer.

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1. The method of oxidizing an organic material in an oxidizer, which comprises: forming a mixture of said organic material with water and a fluid comprising oxygen under conditions near supercritical including a pressure at least about 220 atmospheres, and at the inlet of said oxidizer, causing s

1. The method of oxidizing an organic material in an oxidizer, which comprises: forming a mixture of said organic material with water and a fluid comprising oxygen under conditions near supercritical including a pressure at least about 220 atmospheres, and at the inlet of said oxidizer, causing said mixture to undergo reaction under supercritical conditions for water, characterized by a temperature of at least about 400° C. and a pressure of at least about 220 atmospheres in said oxidizer. 2. The method of claim 1 wherein said temperature is at least about 500° C. and the destruction efficiency of said organic materials is at least about 99.9%. 3. The method of claim 1 wherein said temperature is at least about 600° C. and the destruction efficiency of said organic materials is at least about 99.99%. 4. The method of claims 2 or 3 wherein said organic material comprises chlorinated hydrocarbons. 5. The method of claim 1 wherein the conditions in said oxidizer are adapted to obtain a temperature of at least 450° C. in an effluent stream from said oxidizer and under said conditions removing inorganic salts as particulates therefrom. 6. The method of claim 5 wherein said inorganic salts are soluble in water below the supercritical conditions for water. 7. The method of claim 1 in which said conditions are characterized by a temperature of over about 450° C. 8. The method of claim 7 in which said organic material contains at least one element selected from the group consisting of chlorine, nitrogen, sulfur and phosphorous, and the resulting reaction products of said reaction include chloride ion or an oxy-anion of nitrogen, sulfur or phosphorous. 9. The method of claim 8 in which said reaction products are further reacted with a cation to form an inorganic salt. 10. The method of claim 9 in which said cation is selected from the group consisting of sodium, potassium, magnesium, iron and calcium. 11. The method of claim 7 wherein said organic material comprises at least one chlorinated hydrocarbon which is brought into contact with sodium hydroxide sufficient to provide at least an amount of sodium to form sodium chloride with the elemental chlorine in said hydrocarbon. 12. The method of claim 11 wherein said contact is prior to forming said mixture. 13. The method of claim 12 wherein a mixture is formed of said organic material and water, said sodium hydroxide is added thereto, and then a fluid comprising oxygen is added to said mixture. 14. The method of claim 1 in which said organic material comprises a nitrogen-containing compound. 15. The method of claim 14 in which said nitrogen-containing compound is urea. 16. The method of claims 14 or 15 wherein said conditions include a temperature of at least 550° C. to oxidize said nitrogen-containing compound to substantially nitrogen, carbon dioxide and water. 17. A method according to claim 1 wherein said mixture is formed using water at a temperature and pressure above about 377° C. and 220 atmospheres. 18. A method according to claim 17 wherein the water used has a temperature of at least about 400° C. 19. A method according to claim 17 wherein the water used has a temperature of at least about 500° C. 20. A method according to claim 17 wherein the water used has a temperature of at least about 600° C. 21. A method according to claim 1 wherein an aqueous liquid at supercritical conditions is mixed directly with said organic material and oxygen to quickly bring the mixture to supercritical conditions. 22. A method according to claim 21 wherein the mixture is formed at the inlet of said oxidizer and the temperature of the mixture substantially instantaneously reaches supercritical temperature. 23. A method according to claim 1 wherein the residence time of the mixture in the oxidizer is from about less than one minute to about 5 minutes. 24. A method according to claim 23 wherein the residence time is less than about one minute. 25. The method of oxidizing an organic material, which comprises: forming a mixture of said organic material with water and a fluid comprising oxygen under conditions near supercritical including a pressure of at least about 220 atmospheres, at the inlet of said oxidizer, causing said mixture to undergo reaction under supercritical conditions for water, and conducting said reaction under conditions to provide an effluent stream at a temperature above about 450° C. to cause inorganics therein to precipitate. 26. The method of claim 25 in which said organic material contains at least one element selected from the group consisting of chlorine, nitrogen, sulfur and phosphorous, and the resulting reaction products of said reaction include chloride ion or an oxy-anion of nitrogen, sulfur or phosphorous. 27. The method of claim 26 wherein a compound containing a cation is added to said effluent to form an inorganic salt which precipitates therefrom. 28. The method of claim 27 wherein said cation is selected from the group consisting of sodium, potassium, magnesium, iron and calcium. 29. The method of claim 25 in which said organic material is a chlorinated hydrocarbon and sodium hydroxide is added thereto prior to oxidizing said organic material, wherein the amount of sodium hydroxide added is at least about equivalent to that needed to form a salt with the free chloride ions released from oxidizing said organic material. 30. The method of removing inorganics from oxidized organic materials which comprises providing for the precipitation of inorganic salts by contacting said oxidized materials with a fluid at a temperature of at least about 450° C. and a pressure of at least 220 atmospheres, and separating said inorganic salts therefrom. 31. The method of claim 30 wherein said oxidized organic materials contain the oxidation product of an organic material having at least one element selected from the group consisting of chlorine, nitrogen, sulfur and phosphorous. 32. The method of claim 30 wherein said oxidized organic materials contain chloride ions. 33. The method of claims 31 or 32 wherein said oxidized organic materials are treated with a cation to form an inorganic salt. 34. The process of claim 30 wherein said oxidized organic material is made from a process of forming a mixture of organic material, water and an oxygen-containing fluid under conditions near supercritical including a pressure of at least about 220 atmospheres, and at the inlet of the oxidizer causing said mixture to undergo reaction under supercritical conditions for water. 35. The method of claims 1 or 7 or 25 or 34 in which the step of forming said mixture comprises mixing together said organic material and water under supercritical conditions and adding thereto a fluid comprising oxygen. 36. The method or claims 1 or 7 or 25 or 34 wherein the amount of oxygen is at least about stoichiometrically equivalent to that which would completely oxidize said organic material. 37. The method of claims 1 or 7 or 25 or 34 wherein the amount of oxygen is less than the stoichiometrically equivalent to that which would completely oxidize said organic material.