Methods of upgrading biooil to transportation grade hydrocarbon fuels
US-9896390-B2 · Feb 20, 2018 · US
US11692148B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11692148-B2 |
| Application number | US-201816765991-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 22, 2018 |
| Priority date | Nov 27, 2017 |
| Publication date | Jul 4, 2023 |
| Grant date | Jul 4, 2023 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A method is disclosed for preparing a renewable fuel blend. The method includes subjecting at least two feedstocks of different biological origins to catalytic cracking in a catalytic cracking unit and to hydrotreatment in a hydrotreatment unit to form a fuel blend having an aromatic hydrocarbon content from 26 to 42 wt-% and a paraffinic hydrocarbon content of less than 53 wt-%, as measured according to ASTM D2425-04 (2011). The fuel blend is formed by mixing the at least two feedstocks together before subjecting them to the catalytic cracking and hydrotreatment, or by obtaining a first fuel component and at least one further fuel component from the catalytic cracking and hydrotreatment of the at least two feedstocks, and mixing the first fuel component and the at least one further fuel component together.
Opening claim text (preview).
The invention claimed is: 1. A method for preparing a renewable diesel fuel blend, the method comprising: subjecting at least two different feedstocks of renewable biological origin, the at least two different feedstocks including a feedstock for obtaining a first fuel component and a feedstock for obtaining a further fuel component, to catalytic cracking in a catalytic cracking unit and to hydrotreatment in a hydrotreatment unit to form a renewable diesel fuel blend having an aromatic hydrocarbon content from 26 to 42 wt-% and a paraffinic hydrocarbon content of less than 53 wt-%, as measured according to ASTM D2425-04 (2011); wherein the feedstock for obtaining the first fuel component of the renewable diesel fuel blend is tall oil pitch (TOP), and the feedstock for obtaining the further fuel component of the renewable diesel fuel blend includes at least one of used cooking oil (UCO) and animal fat (AF), wherein the formed renewable diesel fuel blend contains 25-75 wt-% first fuel component obtained from tall oil pitch (TOP), and 25-75 wt-% further fuel component obtained from at least one of used cooking oil (UCO) and animal fat (AF), wherein the renewable diesel fuel blend is formed by: obtaining the first fuel component and the further fuel component from the catalytic cracking and hydrotreatment of the at least two feedstocks, and mixing said first fuel component and said further fuel component together; and wherein a measured cloud point of the renewable diesel fuel blend is lower than a calculated cloud point of the fuel blend as a weighted mean of measured cloud points of individual components thereof, the individual components being the first fuel component and the at least one further fuel component, wherein the measured cloud points are measured according to ASTM D7689-11 (2012). 2. The method according to claim 1 , wherein 33 wt-% or more of the paraffinic hydrocarbon content of the renewable diesel fuel blend is i-paraffins. 3. The method according to claim 1 , wherein at least one of a first fuel component or at least one further fuel component of the renewable diesel fuel blend is a renewable middle distillate fuel component having a distillation range from 160° C. to 370° C. 4. The method as claimed in claim 1 , wherein the catalytic cracking comprises: thermofor catalytic cracking (TCC). 5. The method as claimed in claim 1 , wherein the hydrotreatment is performed at a temperature from 200° C. to 400° C. and at a pressure from 20 bar to 150 bar in a presence of a hydrotreatment catalyst. 6. The method as claimed in claim 1 , wherein the method comprises: subjecting at least one of a first fuel component or a further fuel component to isomerization. 7. The method as claimed in claim 1 , wherein the catalyst in the catalytic cracking includes at least one of aluminium based catalyst, lanthanum based catalyst, titanium based catalyst or silicon based catalyst. 8. The method as claimed in claim 1 , wherein the temperature in the catalytic cracking is from 450° C. to 470° C. 9. The method as claimed in claim 1 , wherein the method comprises: subjecting the feedstock having animal fat to pretreatment before the catalytic cracking by at least one of adsorption, treatment with an ion exchange resin, or washing. 10. The method as claimed in claim 1 , wherein the method comprises: subjecting a first and a further fuel component to fractionation by distillation. 11. The method according to claim 1 , wherein 33 to 40 wt-% or more of the paraffinic hydrocarbon content of the renewable diesel fuel blend is i-paraffins. 12. The method according to claim 2 , wherein at least one of a first fuel component or at least one further fuel component of the renewable diesel fuel blend is a renewable middle distillate fuel component having a distillation range from 180° C. to 360° C. 13. The method as claimed in claim 1 , wherein the temperature in the catalytic cracking is from 455° C. to 465° C. 14. The method as claimed in claim 1 , wherein the renewable diesel fuel blend has a cloud point that is lowered by approximately 20-30% than the cloud points of the individual fuel components. 15. A method for preparing a renewable diesel fuel blend, the method comprising: subjecting at least two different feedstocks of renewable biological origin, the at least two different feedstocks including a feedstock for obtaining a first fuel component and a feedstock for obtaining a further fuel component, to catalytic cracking in a catalytic cracking unit and to hydrotreatment in a hydrotreatment unit to form a renewable diesel fuel blend having an aromatic hydrocarbon content from 26 to 42 wt-% and a paraffinic hydrocarbon content of less than 53 wt-%, as measured according to ASTM D2425-04 (2011); wherein the feedstock for obtaining the first fuel component of the renewable diesel fuel blend is tall oil pitch (TOP), and the feedstock for obtaining the further fuel component of the renewable diesel fuel blend includes at least one of used cooking oil (UCO) and animal fat (AF), wherein the formed renewable diesel fuel blend contains 25-75 wt-% first fuel component obtained from tall oil pitch (TOP), and 25-75 wt-% further fuel component obtained from at least one of used cooking oil (UCO) and animal fat (AF), wherein the renewable diesel fuel blend is formed by: mixing the at least two feedstocks together before subjecting them to the catalytic cracking and hydrotreatment; and wherein a measured cloud point of the renewable diesel fuel blend is lower than a calculated cloud point of the fuel blend as a weighted mean of measured cloud points of individual components thereof, the individual components being the first fuel component and the at least one further fuel component, wherein the measured cloud points are measured according to ASTM D7689-11 (2012).
of animal origin · CPC title
Used oils · CPC title
plural parallel stages only · CPC title
Alkanes · CPC title
characterised by the catalyst used · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.