Claims
- 1. A process for the selective production of hydrogen bromide directly from ammonium bromide which consists essentially of contacting ammonium bromide and an oxygen containing gas, at a molar ratio of oxygen to bromide of less than 1, with an inorganic oxidation catalyst containing at least one element selected from the group consisting of rhenium, a noble metal of the 8th Subgroup of the Periodic Table and carbon, and mixtures thereof, reacting said ammonium bromide and oxygen in the presence of said catalyst at about ambient pressure and a temperature of from 200 to 800.degree. C. and a reaction time of more than 0.1 second to produce a reaction gas product consisting predominantly of hydrogen bromide, nitrogen and H.sub.2 O and recovering hydrogen bromide from said reaction gas product.
- 2. The process of claim 1 wherein the catalyst contains additionally at least one compound of an element of the first to fourth main group and/or at least a compound of an element of the second to fourth subgroup of the Periodic Table.
- 3. The process of claim 1 wherein the catalyst is used on a carrier in elementary form or as a compound.
- 4. The process of claim 1 wherein the reaction is carried out at a temperature of from 250.degree. to 700.degree. C.
- 5. The process of claim 1 wherein the reaction is carried out at a temperature of from 300.degree. to 600.degree. C.
- 6. The process of claim 1 wherein the reaction is carried out in 0.5 second to 5 minutes.
- 7. The process of claim 1 wherein an oxygen containing gas is passed through a mixture of ammonium bromide and catalyst.
- 8. The process of claim 1 wherein a gaseous mixture of ammonium bromide and an oxygen containing gas are passed over the catalyst.
- 9. The process of claim 1 wherein the catalyst contains at least one element selected from ythe group consisting of ruthenium, rhodium, iridium and platinum.
- 10. The process of claim 1 wherein the oxidation catalyst comprises rhenium.
- 11. The process of claim 1 wherein the oxidation catalyst comprises ruthenium.
- 12. The process of claim 1 wherein the oxidation catalyst comprises rhodium.
- 13. The process of claim 1 wherein the oxidation catalyst comprises platinum.
- 14. The process of claim 1 wherein the oxidation catalyst comprises iridium.
- 15. The process of claim 13 wherein the oxidation catalyst comprises carbon.
- 16. A process for the selective production of hydrogen bromide directly from ammonium bromide which consists essentially of contacting ammonium bromide and an oxygen containing gas, at a molar ratio of oxygen to bromide of less than 1, with an inorganic catalyst containing at least one element selected from the group consisting of active charcoal, ruthenium, rhodium, platinum, rhenium and iridium, reacting said ammonium bromide and oxygen in the presence of said catalyst at about ambient pressure and a temperature of from 300.degree. to 600.degree. C. and a reaction time of 0.5 second to 5 minutes to produce a reaction gas product consisting essentially of hydrogen bromide, nitrogen and H.sub.2 O and recovering hydrogen bromide from said reaction gas product.
- 17. The process of claim 16 wherein the oxidation catalyst comprises ruthenium.
- 18. The process of claim 16 wherein the oxidation catalyst comprises rhodium.
- 19. The process of claim 16 wherein the oxidation catalyst comprises platinum.
- 20. The process of claim 16 wherein the oxidation catalyst comprises rhenium.
- 21. The process of claim 16 wherein the oxidation catalyst comprises iridium.
- 22. The process of claim 16 wherein the oxidation catalyst comprises active charcoal.
Priority Claims (1)
Number |
Date |
Country |
Kind |
2404335 |
Jan 1974 |
DEX |
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Parent Case Info
This is a division, of application Serial No. 544,915 filed Jan. 28, 1975.
US Referenced Citations (1)
Number |
Name |
Date |
Kind |
3103419 |
Hunter et al. |
Sep 1963 |
|
Divisions (1)
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Number |
Date |
Country |
Parent |
544915 |
Jan 1975 |
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