Halogen mediated production of hydrogen and carbon from hydrocarbons
US-2025313459-A1 · Oct 9, 2025 · US
US11713244B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11713244-B2 |
| Application number | US-201916525829-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 30, 2019 |
| Priority date | Aug 2, 2018 |
| Publication date | Aug 1, 2023 |
| Grant date | Aug 1, 2023 |
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To provide a method that enables production of bromine in good yield. A method for producing bromine includes: a step of supplying a gas containing a bromine compound and a gas containing oxygen to a reactor that includes a catalyst packed bed, and oxidizing the bromine compound to obtain a gas containing bromine, in which the step satisfies the following 0.30≤a≤0.55 and 0.40≤L1≤6.0; where “a” represents porosity [−] of the catalyst packed bed, and “L1” is defined by the following Formula (3): Formula (3) L1=L2V/(P(aV+b))×(T+273.14)/273.14; wherein L2: Superficial velocity of reaction gas [m/s]; LP: Reaction pressure [atm]; T: Reaction temperature [° C.]; V: Reactor volume corresponding to catalyst packed bed [L]; a: Porosity of catalyst packed bed [−] and b: Pore volume of catalyst packed bed [L].
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What is claimed is: 1. A method for producing bromine, comprising a step of supplying a gas containing a bromine compound and a gas containing oxygen to a reactor that includes a catalyst packed bed, and oxidizing the bromine compound to obtain a gas containing bromine, wherein the step satisfies the following Inequality (1) and Inequality (2): 0.30≤ a≤ 0.55 Inequality (1) 0.40≤ L 1≤6.0 Inequality (2) where “a” represents porosity [−] of the catalyst packed bed, and “L1” is defined by the following Formula (3): L 1= L 2 V /( P ( aV+b ))×( T+ 273.14)/273.14 Formula (3) L2: Superficial velocity of reaction gas [m/s] P: Reaction pressure [atm] T: Reaction temperature [° C.] V: Reactor volume corresponding to catalyst packed bed [L] a: Porosity of catalyst packed bed [−] b: Pore volume of catalyst packed bed [L]. 2. The method for producing bromine according to claim 1 , wherein the bromine compound is hydrogen bromide. 3. The method for producing bromine according to claim 1 , wherein the bromine compound in an outlet of the reactor has a conversion of 90% or more. 4. The method for producing bromine according to claim 1 , wherein a temperature at an outlet of the reactor is 250° C. to 400° C. 5. The method for producing bromine according to claim 1 , wherein the catalyst is at least one type of metal or metal compound selected from the group consisting of ruthenium, a compound of ruthenium, copper, a compound of copper, titanium, and a compound of titanium. 6. The method for producing bromine according to claim 1 , wherein the reactor is an adiabatic reactor. 7. The method for producing bromine according to claim 1 , wherein the reactor includes two or more catalyst packed beds connected in series. 8. The method for producing bromine according to claim 7 , wherein a temperature at an outlet of the lowermost catalyst packed bed with respect to a flow direction of the gas containing a bromine compound is lower than a temperature at an outlet of the catalyst packed bed of immediately upstream side of the lowermost catalyst packed bed. 9. The method for producing bromine according to claim 7 , wherein the uppermost catalyst packed bed with respect to a flow direction of the gas containing a bromine compound includes titanium oxide as a catalyst, and the lowermost catalyst packed bed with respect to a flow direction of the gas containing a bromine compound includes at least one selected from the group consisting of metallic ruthenium and a ruthenium compound as a catalyst. 10. The method for producing bromine according to claim 7 , further comprising supplying the gas containing oxygen to each catalyst packed bed.
Bromine · CPC title
placed in series · CPC title
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