Fluidizable vanadium catalyst for oxidative dehydrogenation of alkanes to olefins in a gas phase oxygen free environment
US-2017354955-A1 · Dec 14, 2017 · US
US11724974B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11724974-B2 |
| Application number | US-201917271139-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 27, 2019 |
| Priority date | Aug 31, 2018 |
| Publication date | Aug 15, 2023 |
| Grant date | Aug 15, 2023 |
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According to one or more embodiments described herein, a method for dehydrogenating hydrocarbons may include passing a hydrocarbon feed comprising one or more alkanes or alkyl aromatics into a fluidized bed reactor, contacting the hydrocarbon feed with a dehydrogenation catalyst in the fluidized bed reactor to produce a dehydrogenated product and hydrogen, and contacting the hydrogen with an oxygen-rich oxygen carrier material in the fluidized bed reactor to combust the hydrogen and form an oxygen-diminished oxygen carrier material. In additional embodiments, a dual-purpose material may be utilized which has dehydrogenation catalyst and oxygen carrying functionality.
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The invention claimed is: 1. A method for dehydrogenating hydrocarbons comprising: passing a hydrocarbon feed comprising one or more alkanes or alkyl aromatics into a first fluidized bed reactor, wherein at least 95 wt. % of the hydrocarbon feed has an atmospheric boiling point of less than or equal to 300° C.; contacting the hydrocarbon feed with a dehydrogenation catalyst in the first fluidized bed reactor to produce a dehydrogenation effluent comprising hydrogen; passing the dehydrogenation effluent to a second fluidized bed reactor, wherein the second fluidized bed reactor comprises an oxygen-rich oxygen carrier material, and wherein the oxygen-rich oxygen carrier is reducible; contacting the hydrogen of the dehydrogenation effluent with the oxygen-rich oxygen carrier material to combust at least a portion of the hydrogen, produce a combustion effluent, and form an oxygen-diminished oxygen carrier material; passing the oxygen-diminished oxygen carrier material to a first regeneration unit; oxidizing the oxygen-diminished oxygen carrier material in the first regeneration unit to form the oxygen-rich oxygen carrier material; and passing the oxygen-rich oxygen carrier material from the first regeneration unit to the second fluidized bed reactor. 2. The method of claim 1 , wherein contacting the hydrogen with the oxygen-rich oxygen carrier material removes from 1 wt. % to 50 wt. % of releasable oxygen from the oxygen-rich oxygen carrier material. 3. The method of claim 1 , wherein the dehydrogenation catalyst in the first fluidized bed reactor is regenerated in a second regeneration unit. 4. The method of claim 1 , further comprising: passing the combustion effluent out of the second fluidized bed reactor to a third fluidized bed reactor comprising the dehydrogenation catalyst, and contacting the combustion effluent with the dehydrogenation catalyst in the third fluidized bed reactor to produce a dehydrogenated product. 5. The method of claim 1 , wherein the oxygen carrier material exhibits Geldart A properties or Geldart B properties.
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