IP Library Patent Application 10523649
Patent Application
App. No. 10/523,649

Fatty acid composition, its production and use

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Patent No.
US None
App. No.
10/523,649
Abstract

The present invention relates to a fatty acid composition which contains an effective amount of fatty acids providing improved low temperature stability of the composition. The present invention also relates to a process for producing a fatty acid composition wherein the process comprises the steps of selecting a crude tall oil having a fatty acid concentration and type capabld of providing low temperature stability, distilling said crude tall oil to provide a fatty acid composition containing an effective amount of tall oil fatty acids providing low temperature stability. The fatty acid composition of the present invention is used as a fuel additive.

Claims (35)

1 . A fatty acid composition characterized in that said composition contains less than 3% saturated fatty acids, more than 10% C18;3 fatty acids, more than 30% C18;2 fatty acids and less than 35% C18;1 fatty acids, said fatty acids providing improved low temperature stability of the composition, and that the cloud point of said fatty acid composition is lower than −4° C., and said composition lacks a paraffine dispergent.

2 . A fatty acid composition according to claim 1 characterized in that said fatty acids are derived from plant sources.

3 . A fatty acid composition according to claim 1 or 2 characterized in that said fatty acids are derived from tall oil or vegetable sources.

4 . A fatty acid composition according to claim 1 , 2 or 3 characterized in that the composition contains less than 1.5% saturated fatty acids and more than 90%, preferably more than 95%, more preferably more than 98% unsaturated fatty acids.

5 . A fatty acid composition according to claim 4 characterized in that the content of the C18;3 fatty acids is more than 15%, preferably more than 20%, more preferably more than 25%.

6 . A fatty acid composition according to claim 5 characterized in that said C18;3 fatty acid is pinolenic acid.

7 . A fatty acid composition according to claim 4 or 5 characterized in that the total content of C16;0, C17;0 and C18;0 fatty acids is less than 2.2%, more preferably less than 1%, most preferably less than 0.5%,

8 . A fatty acid composition according to claim 4 characterized in that the content of C20;0 fatty acids is less than 1%, preferably less than 0.5%.

9 . A fatty acid composition according to claim 4 characterized in that the content of the resin acids is less than 5%, preferably less than 2%, more preferably less than 1%.

10 . A fatty acid composition according to claim 4 characterized in that the content of the C18;2 fatty acids is more than 40%, preferably more than 50%.

11 . A fatty acid composition according to claim 4 characterized in that the content of the C18;1 fatty acids is less than 25%, preferably less than 20%.

12 . A fatty acid composition according to any one of the preceding claims characterized in that the composition contains more than 10%, preferably more than 15% C18;3 fatty acids and more than 30%, preferably more than 40% C18;2 fatty acids and less than 1% preferably less than 0.5% C18;0 fatty acids and less than 2%, preferably less than 1% resin acids and the total of saturated fatty acids is less than 1.5%.

13 . A fatty acid composition according to any one of the preceding claims having a cloud point factor below 0.28 calculated according to the equation I Cp fac =A·[C16;0]+B·[C17;0]+C·[C18;0]+D·[C20;0]+E·[C18;1]+F·[C18;2]+G·[C18;3]+H·[Resin], wherein

[C16;0] means concentration of C16 saturated fatty acids, [C17;0] means concentration of C17 saturated fatty acids, [C18;0] means concentration of C18 saturated fatty acids, [C20;0] means concentration of C20 saturated fatty acids, [C18;1] means concentration of C18 mono-unsaturated fatty acids, [C18;2] means concentration of C18 di-unsaturated fatty acids, [C18;3] means concentration of C18 tri-unsaturated fatty acids, [Resin] means concentration of C16 resin fatty acids and concentration factors are A=6.2, B=1.32, C=34.5, D=0.075, E=1.3, F=−0.27, G=−5.1 and H=17.

14 . A fatty acid composition according to any one of the preceding claims characterized in that the cloud point of said fatty acid composition is lower than −6° C., preferably lower than −10° C., more preferably lower than −15° C., most preferably lower than −20° C.

15 . An ester characterized in that said ester is produced from fatty acid composition according to Claim 1 .

16 . A glycerol ester characterized in that said glycerol ester is produced from fatty acid composition according to claim 1 .

17 . A process for producing a fatty acid composition according to claim 1 characterized in that said process comprises the steps of

selecting a crude tall oil having a fatty acid concentration and type capable of providing low temperature stability

distilling said crude tall oil to provide a fatty acid composition containing an effective amount of tall oil fatty acids providing low temperature stability.

18 . A process according to claim 17 characterized in that selecting includes blending of different crude tall oils.

19 . A process according to claim 17 characterized in that said crude tall oil is derived from trees grown in a cold climate.

20 . A process according to claim 17 characterized in that more than 4% of the fatty acids of the crude tall oil are triple unsaturated fatty acids.

21 . A process according to claim 17 characterized in that less than 1% of the fatty acids of the crude tall oil are saturated fatty acids of C18 or greater.

22 . A process according to claim 13 characterized in that less than 0.3%, preferably less than 0.2%, more preferably less than 0.1% of the fatty acids of the crude tall oil are C18;0 fatty acids.

23 . Use of a fatty acid composition according to claim 1 as a fuel additive.

24 . Use of a fatty acid composition according to claim 1 as a lubricity improver in fuel.

25 . Use according to claim 24 characterized in that said lubricity improver forms a part of a fuel additive package containing other additives.

26 . Use according to claim 25 characterized in that said other additives are one or more of detergent, cold flow additive, antifoam, static dissipate and/or antioxidant.

27 . Use of an ester according to claim 15 or 16 as a fuel additive.

28 . A fuel additive comprising fatty acid composition according to claim 1 characterized in that it is stable at temperature below −4° C.

29 . A fuel containing a fatty acid additive characterized in that said fuel contains an effective amount of a low temperature stable fatty acid lubricity enhancer according to claim 1 which is stable at temperature below −4° C.

30 . A fuel according to claim 29 characterized in that said fuel is diesel, gas oil, gasoline, aviation fuel or kerosene, or a mixture thereof.

31 . A fuel according to claim 29 characterized in that sulfur content of said fuel is less than 500 ppm, preferably less than 350 ppm, more preferably less than 50 ppm, more preferably less than 15 ppm, most preferably less than 10 ppm.

32 . A fuel according to claim 29 characterized in that said fuel contains 10 to 1000 ppm of said fatty acid lubricity enhancer.

Assignments (10)
RELEASE OF SECURITY INTEREST IN INTELLECTUAL PROPERTY COLLATERAL AT REEL/FRAME NO. 33146/0361 Recorded Jan 6, 2016
From: GOLDMAN SACHS BANK USA
To: ARIZONA CHEMICAL COMPANY LLC
Reel/Frame 037451/0169 →
RELEASE OF SECURITY INTEREST IN PATENT RIGHTS Recorded Jan 6, 2016
From: ANTARES CAPITAL LP, AS SUCCESSOR TO GENERAL ELECTRIC CAPITAL CORPORATION
To: ARIZONA CHEMICAL COMPANY LLC
Reel/Frame 037451/0057 →
ASSIGNMENT OF INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded Oct 9, 2015
From: GENERAL ELECTRIC CAPITAL CORPORATION, AS RETIRING AGENT
To: ANTARES CAPITAL LP, AS SUCCESSOR AGENT
Reel/Frame 036827/0443 →
SECURITY INTEREST Recorded Jun 12, 2014
From: ARIZONA CHEMICAL COMPANY LLC
To: GOLDMAN SACHS BANK USA, AS SECOND LIEN COLLATERAL AGENT
Reel/Frame 033146/0361 →
RELEASE OF SECURITY INTEREST Recorded Jun 12, 2014
From: GENERAL ELECTRIC CAPITAL CORPORATION, AS COLLATERAL AGENT
To: ARIZONA CHEMICAL COMPANY LLC
Reel/Frame 033146/0278 →
SECURITY INTEREST Recorded Jun 12, 2014
From: ARIZONA CHEMICAL COMPANY LLC
To: GENERAL ELECTRIC CAPITAL CORPORATION, AS FIRST LIEN COLLATERAL AGENT
Reel/Frame 033146/0333 →
SECURITY AGREEMENT Recorded Jan 7, 2012
From: ARIZONA CHEMICAL COMPANY, LLC
To: GENERAL ELECTRIC CAPITAL CORPORATION, AS COLLATERAL AGENT
Reel/Frame 027497/0465 →
RELEASE OF SECURITY INTEREST Recorded Jan 6, 2012
From: GENERAL ELECTRIC CAPITAL CORPORATION
To: ARIZONA CHEMICAL COMPANY, LLC
Reel/Frame 027489/0030 →
SECURITY AGREEMENT Recorded Feb 2, 2011
From: ARIZONA CHEMICAL COMPANY, LLC
To: GENERAL ELECTRIC CAPITAL CORPORATION, AS COLLATERAL AGENT
Reel/Frame 025734/0383 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 20, 2005
From: BREWER, MARK; KAUTTO, TORBJORN; RAVASKA, MATTI
To: ARIZONA CHEMICAL
Reel/Frame 016822/0479 →