Integrated solvent deasphalting and steam pyrolysis process for direct processing of a crude oil
US-9284497-B2 · Mar 15, 2016 · US
US11420915B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11420915-B2 |
| Application number | US-202016899254-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 11, 2020 |
| Priority date | Jun 11, 2020 |
| Publication date | Aug 23, 2022 |
| Grant date | Aug 23, 2022 |
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A systems and a method for isomerizing a feedstock to form an alpha-olefin product stream are provided. An exemplary method includes calcining the red mud, flowing an olefin feedstock over the red mud in an isomerization reactor, and separating the alpha-olefin from a reactor effluent.
Opening claim text (preview).
What is claimed is: 1. A method for isomerization of olefins comprising: calcining a red mud catalyst; isomerizing an olefin feedstock over the calcined red mud catalyst in a reactor to form an effluent; and separating the effluent to obtain an alpha-olefin stream and an alpha-olefin depleted stream. 2. The method of claim 1 , wherein the olefin feedstock comprises 2-butene and the effluent comprises 1-butene. 3. The method of claim 1 , wherein the calcining is conducted to dry the catalyst, remove volatile gases, or both, at a temperature of between about 500° C. and about 800° C. for between about 10 minutes and about 150 minutes. 4. The method of claim 1 , wherein the calcining is conducted to dry the catalyst, remove volatile gases, or both, at a temperature of between about 600° C. and about 700° C. for between about 30 minutes and about 130 minutes. 5. The method of claim 1 , wherein the calcining is conducted to dry the catalyst, remove volatile gases, or both, at a temperature of about 650° C. for about 45 minutes. 6. The method of claim 1 , further comprising activating the calcined catalyst at a temperature of between about 400° C. and about 700° C. for between about 2 hours and about 6 hours. 7. The method of claim 1 , further comprising activating the calcined catalyst at a temperature of between about 500° C. and about 600° C. for between about 3 hours and about 5 hours. 8. The method of claim 1 , further comprising activating the calcined catalyst at a temperature of about 650° C. for about 4 hours. 9. The method of claim 1 , wherein the olefin feedstock is obtained from an upstream purification system in a refinery. 10. The method of claim 1 , wherein the olefin feedstock has a boiling point range of between about −30° C. and about 40° C. and comprises butene. 11. The method of claim 1 , wherein the olefin feedstock has a boiling point range of between about −20° C. and about 10° C. and comprises butene. 12. The method of claim 1 , wherein the olefin feedstock has a boiling point range of between about −10° C. and about 0° C. and comprises butene. 13. The method of claim 1 , further comprising flowing the feedstock over the red mud at a weight hour space velocity of between about 400 hr −1 and 1300 hr −1 . 14. The method of claim 1 , further comprising flowing the feedstock over the red mud at a weight hour space velocity of between about 650 hr −1 and 1150 hr −1 . 15. The method of claim 1 , further comprising flowing the feedstock over the red mud at a weight hour space velocity of about 900 hr −1 . 16. The method of claim 1 , wherein the separating is performed in a distillation column. 17. The method of claim 1 , wherein the alpha-olefin stream comprises 1-butene and the separating is performed in a distillation column. 18. The method of claim 1 , further comprising passing the alpha-olefin depleted stream to an upstream purification system. 19. The method of claim 1 , further comprising combining the alpha-olefin depleted stream with the olefin feedstock.
with alkali- or alkaline earth metals · CPC title
Decomposition of a metal salt · CPC title
with metal oxides · CPC title
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
Chemical, physical or physico-chemical processes in general; Their relevant apparatus · CPC title
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