US4486457A
Expired / Lapsed
US
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Margarine fat blend, and a process for producing said fat blend
Assignee: Lever Brothers Co
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Filing: 1983-03-09
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Granted: 1984-12-04
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Expires: 2003-03-09
Abstract
Abstract There is disclosed a margarine fat blend comprising a liquid oil and a hardstock predominantly of triglycerides from 2 saturated C 16-18 -fatty acids and 1 saturated C 12-14 -fatty acid. Said hardstock can be used at levels as low as 4% by weight along with liquid oils comprising triglycerides from polyunsaturated fatty acids, for producing diet margarines. A process for producing said margarine fat blend is also disclosed, comprising interesterification of (a) triglycerides rich in C 16-18 -fatty acid residues with (b) triglycerides rich in C 12-14 -fatty acid residues and fractionation of the interesterified mixture.
Inventors
- 👤 Robert Schijf
- 👤 August M. Trommelen
- 👤 Gabriel J. T. Lansbergen
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 03:05
CPC Classifications
C; C11; C11B; C11B7/00; A; A23; A23D; A23D7/00; A23D7/001; A23D7/015; C11C; C11C3/00; C11C3/02; C11C3/04; C11C3/10
Claims Analysis
Total Claims: 26
Claim 1
Independent Claim
158 words
A margarine fat blend comprising: 70-96 wt. % of a liquid oil (i) which at 10° C. is substantially free from crystallized fat; and 4-30 wt. % of a fat (ii) in which 55-100 wt. % of the triglycerides consist of triglycerides (b) predominantly being H 2 M triglycerides having a carbon number ranging from 44 to 48, and 0-45 wt. % of the triglycerides consist of triglycerides (a) being HML, M 3 , M 2 H, M 2 L, HL 2 , ML 2 and L 3 triglycerides having a carbon number ranging from 34 to 42 and triglycerides (c) predominantly being H 3 triglycerides having a carbon number ranging from 50 to 54; wherein H is a saturated or a mono-trans fatty acid residue with 16 or more carbon atoms, M is a saturated fatty acid residue with 12 to 14 carbon atoms, L is a saturated fatty acid residue with less than 12 carbon atoms.
Claim 2
Dependent Claim
158 words
A margarine fat blend comprising: 70-96 wt. % of a liquid oil (i) which at 10° C. is substantially free from crystallized fat; and 4-30 wt. % of a fat (ii) in which 55-100 wt. % of the triglycerides consist of triglycerides (b) predominantly being H 2 M triglycerides having a carbon number ranging from 44 to 48, and 0-45 wt. % of the triglycerides consist of triglycerides (a) being HML, M 3 , M 2 H, M 2 L, HL 2 , ML 2 and L 3 triglycerides having a carbon number ranging from 34 to 42 and triglycerides (c) predominantly being H 3 triglycerides having a carbon number ranging from 50 to 54; wherein H is a saturated or a mono-trans fatty acid residue with 16 or more carbon atoms, M is a saturated fatty acid residue with 12 to 14 carbon atoms, L is a saturated fatty acid residue with less than 12 carbon atoms.
Claim 3
Dependent Claim
23 words
A margarine fat blend according to claim 1, wherein the level of triglycerides (a) in fat (ii) ranges from 0 to 25 wt.%.
Claim 4
Dependent Claim
23 words
A margarine fat blend according to claim 1, wherein the level of triglycerides (c) in fat (ii) ranges from 0 to 20 wt.%.
Claim 5
Dependent Claim
39 words
A margarine fat blend according to claim 1, wherein oil (i) constitutes 88-96 wt.% and fat (ii) constitutes 4-12 wt.% of the total fat blend and the ratio of polyunsaturated to saturated fatty acids ranges from 3.0 to 4.0.
Claim 6
Dependent Claim
29 words
A margarine fat blend according to claim 1, wherein oil (i) consists of triglycerides in which at least 40% of the fatty acid residues are of the polyunsaturated type.
Claim 7
Dependent Claim
30 words
A margarine fat blend according to claim 5, in which oil (i) is selected from the group consisting of sunflower oil, safflower oil, soybean oil, maize oil and rapeseed oil.
Claim 8
Dependent Claim
52 words
A process for producing a fat blend according to claim 1, comprising mixing a liquid oil (i), which at 10° C. is substantially free from crystallized fat, with a fat (ii) in which 55-100% of the triglycerides, comprising of H 2 M triglycerides, have a carbon number ranging from 44 to 48.
Claim 9
Dependent Claim
48 words
A process according to claim 7, wherein fat (ii) is obtained by randomly interesterifying a mixture of triglycerides in which the ratio of saturated C 16-18 -fatty acids to saturated C 12-14 -fatty acids ranges from 0.4 to 8.5, and fractionating the interesterified mixture to obtain fat (ii).
Claim 10
Dependent Claim
26 words
A process according to claim 8, wherein the ratio of saturated C 16-18 -fatty acids to saturated C 12-14 -fatty acids ranges from 1.0 to 3.0.
Claim 11
Dependent Claim
65 words
A process according to claim 8, wherein fat (ii) is produced by randomly interesterifying a partly or fully hydrogenated, fractionated or non-fractionated fat (a) selected from the group consisting of coconut, ouricurum, babassu, palmkernel, tucum and murumuru fat, with a partly or fully hydrogenated, fractionated or non-fractionated fat (b) wherein at least 60% of the saturated fatty acid residues contain 16 or 18 carbon atoms.
Claim 12
Dependent Claim
34 words
A process according to claim 9, wherein a fat (a) has a melting point ranging from 30° to 41° C. and a fat (b) has a melting point ranging from 50° to 71° C.
Claim 13
Dependent Claim
33 words
A process according to claim 10, wherein fat (b) is selected from the group consisting of hydrogenated palm oil, soybean oil, ground nut oil, sunflower oil, rapeseed oil, maize oil and mixtures thereof.
Claim 14
Dependent Claim
22 words
A process according to claim 8, wherein fractionation of the interesterified mixture is carried out in the presence of an organic solvent.
Claim 15
Dependent Claim
16 words
A process according to claim 13, wherein fractionation is carried out in the presence of acetone.
Claim 16
Dependent Claim
66 words
A process according to claim 14, wherein the fractionation is carried out in two steps, the first step being performed at 22°-33° C. to obtain a higher melting stearin fraction which is discarded, and a lower melting olein fraction which is further fractionated at 12°-24° C. to obtain a second stearin containing at least 55% of triglycerides having a carbon number ranging from 44 to 48.
Claim 17
Dependent Claim
23 words
A process according to claim 15, wherein the first step is carried out at 24°-29° C. and the second step at 15°-22° C.
Claim 18
Dependent Claim
68 words
A process according to claim 14, wherein a first fractionation is carried out at 12°-24° C. to yield a higher melting stearin fraction and a lower melting olein fraction and subsequently a second fractionation of the stearin fraction is carried out at 22°-33° C. to yield a second stearin and a second olein containing at least 55% of triglycerides having a carbon number ranging from 44 to 48.
Claim 19
Dependent Claim
32 words
A process according to claim 7, wherein fat (ii) is obtained by esterifying glycerol with a mixture comprising C 12 -, C 14 -, C 16 - and C 18 fatty acids.
Claim 20
Dependent Claim
47 words
A process according to claim 7, wherein in fat (ii) the sum of the level of triglycerides (a) with a carbon number ranging from 34 to 42 and the level of triglycerides (c) with a carbon number ranging from 50 to 54 is up to 45 wt.%.
Claim 21
Dependent Claim
22 words
A process according to claim 19, wherein a fat (ii) has a level of triglycerides (a) ranging from 0 to 25 wt.%.
Claim 22
Dependent Claim
22 words
A process according to claim 19, wherein a fat (ii) has a level of triglycerides (c) ranges from 0 to 20 wt.%.
Claim 23
Dependent Claim
40 words
A process according to claim 7, wherein 88-96 wt.% of oil (i) are mixed with 4-12 wt.% of fat (ii), to obtain a fat blend in which the ratio of polyunsaturated to saturated fatty acids ranges from 3.0 to 4.0.
Claim 24
Dependent Claim
27 words
A process according to claim 8, wherein oil (i) consists of triglycerides in which at least 40% of the fatty acid residues are of the polyunsaturated type.
Claim 25
Dependent Claim
58 words
A process for producing margarines and low-fat spreads, comprising (1) emulsifying an aqueous phase with a fat blend obtained according to claim 8 and (2) cooling and texturizing the emulsion to yield a product having a hardness expressed in C-value of at least 100 g/cm 2 at 5° C. and at least 70 g/cm 2 at 20° C.
Claim 26
Dependent Claim
30 words
A process according to claim 24, wherein the product has a hardness expressed in C-value of 220-400 g/cm 2 at 5° C. and of 100-250 g/cm 2 at 20° C.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-12-04 | 1988-06-04 | 1988-12-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-12-04 | 1992-06-04 | 1992-12-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-12-04 | 1996-06-04 | 1996-12-04 | $7700.00 | Window Closed / Lapsed |