Production of chemical compounds

1. A chemical production system comprising:

a pulse jet combustion chamber having intake ports for entry of a gas mixture, and an igniter to ignite the gas mixture in the combustion chamber;

a nozzle to restrict exit of the ignited gas mixture from the combustion chamber; and

an expansion chamber to cool the ignited gas with a cooling agent, the expansion chamber having an exhaust where the cooled gas exits the expansion chamber, wherein the gas mixture is selected as a precursor to produce a chemical compound product in the expansion chamber.

2. The system of claim 1 , wherein the combustion chamber reacts the gas mixture with at least oxygen and hydrogen at high temperature and high pressure.

3. The system of claim 1 , wherein the combustion chamber reacts the gas mixture with at least oxygen, nitrogen, and hydrogen at high temperature and high pressure.

4. The system of claim 1 wherein the gas mixture includes a nitrogen source, a hydrogen source, and an oxygen source, and wherein the chemical compound product is nitrogen -based.

5. The system of claim 1 , wherein the gas mixture includes carbon dioxide, and wherein the chemical compound product is methane and other higher order hydrocarbons, and wherein admitted materials further comprise liquids and gases including alkanes to produce polyethylene and used in chemical production under high pressure.

6. The system of claim 1 , wherein the chemical compound product includes both gas and aqueous solution.

7. The system of claim 1 , further comprising a catalyst in the combustion chamber.

8. The system of claim 1 , wherein pollutants are admitted to the combustion chamber to render the pollutants inert following reaction in the combustion chamber.

9. The system of claim 1 , wherein the combustion chamber is used to reform natural gas.

10. A method comprising:

igniting a gas mixture from a hydrogen pulse jet combustion chamber;

restricting exit of the ignited gas mixture from the combustion chamber to increase temperature and pressure;

cooling the ignited gas in an expansion chamber; and

collecting a chemical compound product from the expansion chamber.

11. The method of claim 10 , further comprising forming a catalyst in the combustion chamber during reaction of the gas mixture.

12. The method of claim 10 , further comprising steam reformation of any hydrocarbon into hydrogen with residual including carbon, CO, CO 2 and other hydrocarbons.

13. The method of claim 10 , further comprising reformation of coal and petroleum into hydrogen and residual atomized solid or liquid.

14. The method of claim 13 , wherein the residual is separated and removed from the hydrogen.

15. The method of claim 14 , wherein the residual is used as in asphalt or other building material.

16. The method of claim 10 , further comprising admitting to the combustion chamber, pollutants from power production or industrial chemical production, and rendering the pollutants inert following reaction in the combustion chamber.

17. The method of claim 10 , further comprising admitting vapor or mist to the combustion chamber to modify combustion.

18. The method of claim 10 , further comprising admitting fine ground coal to the combustion chamber to release residue.

19. The method of claim 10 , further comprising reforming natural gas in the combustion chamber.

20. A method comprising:

igniting a gas mixture in a combustion chamber;

admitting vapor or mist to the combustion chamber to modify combustion product;

restricting exit of the ignited gas mixture from the combustion chamber to increase pressure; and

collecting a chemical compound product from the expansion chamber.