Fatty acid composition

Patent metadata

Field	Value
Publication number	US-2018010051-A1
Application number	US-201615545408-A
Country	US
Kind code	A1
Filing date	Feb 9, 2016
Priority date	Feb 9, 2015
Publication date	Jan 11, 2018
Grant date	—

Abstract

This disclosure relates to the field of renewable oil compositions and to the use of renewable oil compositions for production of hydrocarbon compositions, which can be used for traffic fuels and other solutions. An exemplary composition contains free fatty acids and triglycerides, in a concentration of free fatty acids from 15 wt-% to 80 wt-% and a remainder being predominantly triglycerides. A method for producing hydrocarbons from a renewable oil feedstock, in which the feedstock which contains free fatty acids from 15 wt-% to 80 wt-%, and a remainder being predominantly triglycerides, is subjected to a pretreatment process followed by a hydrotreatment process for obtaining hydrocarbons.

First claim

1 . A method for producing hydrocarbons from a renewable oil feedstock, comprising:
subjecting the feedstock to a pretreatment process to form a pretreated feedstock; subjecting said pretreated feedstock to a hydrotreatment process; and obtaining hydrocarbons from said hydrotreatment process,
wherein said feedstock contains free fatty acids from 15 wt-% to 80 wt-% of a total feedstock weight, and a remainder being predominantly triglycerides.

2 . The method according to claim 1 , wherein said feedstock comprises:
free fatty acids from 20 wt-% to 50 wt-%, of the total feedstock weight, and a remainder being predominantly triglycerides.

3 . The method according to claim 1 , wherein said feedstock comprises:
free fatty acids from 50 wt-% to 80 wt-%, of the total feedstock weight, and a remainder being predominantly triglycerides.

4 . The method according to claim 1 , wherein said pretreatment process comprises:
a filtration step.

5 . The method according to claim 1 , wherein said pretreatment process is a purification process for removing impurities that include phospholipids, metals and solids.

6 . The method according to claim 1 , wherein said hydrotreatment process is a catalytic hydrodeoxygenation process using a metal catalyst wherein said metal is selected from the group consisting of Fe, Pd, Pt, Ni, Mo, Co, Ru, Rh, W and any combination thereof.

7 . The method according to claim 1 , wherein said feedstock is a mixture comprising:
vegetable oil, animal fat or a mixture thereof; and a free fatty acid stream selected from palm fatty acid distillate (PFAD), sludge palm oil (SPO), crude tall oil (CTO), crude fatty oil (CFO), tall oil fatty acid (TOFA), acid oils, free fatty acid side streams from oleochemistry, lauric fatty acid, palm kernel fatty acid, brown grease, and any mixture thereof.

8 . A composition comprising:
free fatty acids and triglycerides, wherein the concentration of free fatty acids is from 15 wt-% to 80 wt-% of a total feedstock weight and a remainder being predominantly triglycerides.

9 . The composition according to claim 8 , wherein said triglyceride source is selected from vegetable oil, animal fat or a mixture thereof; and
said fatty acid source is selected from palm fatty acid distillate (PFAD), sludge palm oil (SPO), crude tall oil (CTO), crude fatty oil (CFO), tall oil fatty acid (TOFA), acid oils, free fatty acid side streams from oleochemistry, lauric fatty acid, palm kernel fatty acid, brown grease, and any mixture thereof.

10 . (canceled)

11 . The method according to claim 1 , wherein said feedstock contains free fatty acids from 20 wt-% to 80%-wt and a remainder being predominantly triglycerides.

12 . The method according to claim 6 , comprising:
Performing the method on a support selected from aluminum, silica and active carbon.

13 . The composition according to claim 8 , wherein said feedstock contains free fatty acids from 20 wt-% to 80%-wt and a remainder being predominantly triglycerides.

14 . The composition according to claim 13 , wherein said triglyceride source is selected from vegetable oil, animal fat or a mixture thereof; and
said fatty acid source is selected from palm fatty acid distillate (PFAD), sludge palm oil (SPO), crude tall oil (CTO), crude fatty oil (CFO), tall oil fatty acid (TOFA), acid oils, free fatty acid side streams from oleochemistry, lauric fatty acid, palm kernel fatty acid, brown grease, and any mixture thereof.

15 . The method according to claim 4 , wherein said hydrotreatment process is a catalytic hydrodeoxygenation process using a metal catalyst wherein said metal is selected from the group consisting of Fe, Pd, Pt, Ni, Mo, Co, Ru, Rh, W and any combination thereof.

16 . The method according to claim 4 , wherein said feedstock is a mixture comprising:
vegetable oil, animal fat or a mixture thereof; and a free fatty acid stream selected from palm fatty acid distillate (PFAD), sludge palm oil (SPO), crude tall oil (CTO), crude fatty oil (CFO), tall oil fatty acid (TOFA), acid oils, free fatty acid side streams from oleochemistry, lauric fatty acid, palm kernel fatty acid, brown grease, and any mixture thereof.

Assignees

• Neste Oyj

Inventors

• Lindqvist Petri
• Lehtimaa Tuula
• Sippola Väinö
• Lehtinen Olli-Pekka
• Faaij Gerard

Classifications

• C10G45/00

  Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds · CPC title

• C11C3/12

  by hydrogenation · CPC title

• C11B3/008

  by filtration, e.g. including ultra filtration, dialysis (C11B3/005 takes precedence) · CPC title

• C10G3/50 Primary

  in the presence of hydrogen, hydrogen donors or hydrogen generating compounds · CPC title

• C11B1/02

  Pretreatment · CPC title