Mercury and silicon removal from plastic-derived pyrolysis oil
US-2024101914-A1 · Mar 28, 2024 · US
US10190062B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10190062-B2 |
| Application number | US-201615199122-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 30, 2016 |
| Priority date | Jul 2, 2015 |
| Publication date | Jan 29, 2019 |
| Grant date | Jan 29, 2019 |
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Methods for preparing, converting, and/or transporting bitumen are provided. Asphaltene prills, prilling processes, and converted bitumen suitable for transport are disclosed. One method for preparing bitumen for transport comprises: separating asphaltene from the bitumen to generate a deasphalted oil and asphaltene; separating the asphaltene into a first asphaltene fraction and a second asphaltene fraction, the first asphaltene fraction being less soluble in deasphalted oil and the second asphaltene fraction being more soluble in deasphalted oil; and forming an asphaltene prill comprising an inner core comprising the second asphaltene fraction and an outer layer comprising the first asphaltene fraction. Asphaltene prills disclosed herein may comprise an inner core comprising an asphaltene fraction having more solubility in deasphalted oil, and an outer layer comprising an asphaltene fraction having less solubility in deasphalted oil. Methods for the transport of bitumen via a pipeline are disclosed.
Opening claim text (preview).
What is claimed is: 1. A method for preparing or converting bitumen for transport, the method comprising: separating asphaltene from the bitumen to generate a deasphalted oil and asphaltene; separating the asphaltene into a first asphaltene fraction and a second asphaltene fraction, the first asphaltene fraction being less soluble in deasphalted oil and the second asphaltene fraction being more soluble in deasphalted oil; and forming an asphaltene prill comprising an inner core comprising the second asphaltene fraction and an outer layer comprising the first asphaltene fraction. 2. The method of claim 1 , further comprising the step of: adding one or more hollow portions to the asphaltene prill to control the density of the asphaltene prill. 3. The of claim 2 , wherein the one or more hollow portions are added to the inner core of the asphaltene prill. 4. The method of claim 1 , further comprising the step of: combining the asphaltene prill with the deasphalted oil to form a flowable slurry for transport in a pipeline. 5. The method of claim 4 , wherein the slurry has increased flowability relative an asphaltene prill absent the deasphalted oil. 6. The method of claim 4 , wherein one or more additional diluents are added to the slurry. 7. The method of claim 4 , wherein the slurry has increased flowability relative a bitumen diluted with diluent. 8. The method according to claim 1 , further comprising a step of: visbreaking the deasphalted oil to reduce the viscosity of the oil. 9. A method for transporting a bitumen in a pipeline, the method comprising: separating asphaltene from the bitumen to generate a deasphalted oil and asphaltene; separating the asphaltene into a first asphaltene fraction and a second asphaltene fraction, the first asphaltene fraction being less soluble in deasphalted oil and the second asphaltene fraction being more soluble in deasphalted oil; forming an asphaltene prill comprising an inner core comprising the second asphaltene fraction and an outer layer comprising the first asphaltene fraction; combining the asphaltene prill with the deasphalted oil to form a flowable slurry suitable for transport in a pipeline; and transporting the slurry in a pipeline. 10. The method of claim 9 , further comprising a step of: adding one or more hollow portions to the asphaltene prill to control the density of the asphaltene prill. 11. The method of claim 10 , wherein the one or more hollow portions are added to the inner core of the asphaltene prill. 12. The method of claim 9 , wherein one or more additional diluents are added to the slurry. 13. The method of claim 9 , further comprising a step of: visbreaking the deasphalted oil to reduce the viscosity of the oil.
including at least one thermal cracking step · CPC title
Solvent de-asphalting · CPC title
for solids or suspensions of solids in liquids, e.g. slurries (F17D1/086 takes precedence) · CPC title
Solidifying, Disintegrating, e.g. granulating · CPC title
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