A METHOD FOR PREPARING A HARDSTOCK, A HARDSTOCK AND A PLASTIC FAT SPREAD COMPRISING SUCH A HARDSTOCK

Abstract: Fully hardened, but otherwise not chemically treated fat material usable as a hardstock having the following fatty acid composition: C12 9-45 wt.%, C14 1-5 %, C16 3-7 %, C18 >40 %, others up to 10 %; these fatty acids being arranged in the following triglyceride combinations: H3 0-35 wt.%, HHM 20-80 %, MHM 10-60 %, M3 0-10 %, H representing saturated fatty acids having more than 15 carbon atoms and M saturated acids having 12 or 14 carbon atoms, the sequence of the symbols H and M representing the position of the fatty acids in the triglyceride molecule. A process for producing such fat material and spreads and shortening comprising such fat materials.

Description: A method for preparing a hardstoc , a hardstock and a plastic fat spread comprising such a hardstock The invention relates to a fat usable as a hardstock in plastic fat spreads and a method for preparing such a hardstock. Plastic fat spreads are usually composed of an aqueous phase and a fat phase, the latter nowadays comprising a liquid base stock and a smaller amount of a hardstock for structuring the fat phase to give the spread the required plasticity and spreadability. For nutritional, health and naturalness reasons several requirements are to be pursued - smallest possible amount of saturated fat - smallest possible amount of trans unsaturated fat - highest possible amount of cis unsaturated fat, especially of all-cis polyunsaturated fat - no use of so called tropical oils - minimum processing, especially minimum use of chemical treatments. For satisfying these requirements as far as possible a major measure is using a hardstock having a very efficient structuring capacity whereby a relatively low percentage of hardstock calculated on total fat can be used. EP 89 082 describes hardstocks that can be used at relatively low amounts in the fat blend of margarines and spreads. At least 55 wt% of the hardstock consists of triglycerides with a carbon number ranging from 44 to 48. These triglycerides comprise predominantly 2 saturated or mono-trans fatty acids with a chain length of 16 or more carbon atoms (indicated by "H") and 1 lauric or myristic fatty acid (indicated by "M") . The hardstock can be prepared by randomly esterifying appropriate fatty acids with glycerol or by randomly interesterifying mixtures of fats such as fully hardened palm kernel fat and palm fat and fractionating the randomized mixture to recover a fraction enriched in the socalled H 2 M triglycerides. EP 233 036 discloses hardstocks given by the expression Z 2 = 4XY where X = HHH, Y = MHM and Z = HHM. The α(l,3) fatty acids must be randomly distributed which is achieved by means of enzymatic rearrangement of a fat mixture. As source of M acids, tropical oils like coconut, palm kernel and babassu oil are used. According to the present invention the above requirements are highly met by a fully hardened, but otherwise not chemically treated fat material having the following fatty acid composition: C 12 9-45% C 14 1-5% C 16 3-7% C 18 >40% others 0-10% and preferably 0-5%, these fatty acids being arranged in the following triglyceride combinations: H 3 0-35% HHM 20-80% MHM 10-60% M 3 0-10% H representing saturated fatty acids having more than 15 carbon atoms and M saturated fatty acids having 12 or 14 carbon atoms, the sequence of the symbols H and M representing the position of the fatty acids in the triglyceride molecule. The sequences 123 and 321 are equivalent for the present purposes, e.g. HHM and MHH are considered to be the same and are jointly represented by HHM. In view of the prescribed fatty acid composition, M consists largely of C 12 with only a small amount of C 14 , H consists mainly of C 18 , a small amount of C 16 , and possibly a minor amount of C 2 o*-C 24 acids. Preferably the combined amount of H 3 , HHM, MHM and M 3 triglycerides is at least 85%, more preferably 90-100%. All percentages are percentage by weight. Preferably the triglycerides are present in the following combinations: H 3 2 -25% more preferably 5-15% HHM 30-80 40-75% MHM 10-50 10-30% Preferably the C 12 content is 10-45%, more preferably 18- 40%, the C 16 content is preferably 3-5% and the C 18 content is preferably 50-70%. The invention also relates to a process for producing a fat material usable as a hardstock, said process not involving a blending or (inter)esterification step, by fully hardening an oil having (a) 9-55% of lauric acid, (b) 20- 55% of oleic acid, (c) less than 12 % of saturated C 14.18 fatty acids and (d) 15 to 35 % of linolenic and linoleic acid; the total of (a) to (d) being more than 90% and preferably more than 95% and optionally fractionating the fully hardened oil and recovering at least one of the fractions. The oil used for this process can conveniently be derived from suitably selected brassica seed, for example as described in WO 92/20236. The oil preferably contains 10-45%, more preferably 18-40% of lauric acid, the content of C 14 . 16 saturated fatty acids is preferaby 4-10%. The invention also relates to a hardstock material obtainable by one of the preceding processes. Preferably, the fat material of the present invention described above is prepared by means of the present process, with or without a fractionation step. The hardstock materials of the invention have not been subjected to any chemical modification treatments except hardening. This hydrogenation is carried out to completion. Consequently, the hardstock is substantially free from trans fatty acids. By the combination of triglyceride structure and only small amounts of C 14 and C 16 acids an optimum combination is found allowing the formulation of margarines and other spreads with extremely favourable fatty acid profile, as expressed by the Keys number (see below) . No tropical oils need to be used. The hardstock can be prepared using only simple processing without the need for complicated esterification or interesterification equipment or sophisticated blending stations. The invention finally relates to a spread comprising 5-90% fat phase and 95-10% of an aqueous phase, in which the fat phase comprises 4-20%, preferably 6-20% and more preferably 8-14% of a hardstock of claims 1, 2, or 6, the remaining fat being a liquid oil. If necessary the lower percentages may require a fractionation of the hardened fat materials in order to remove the lower melting fractions therefrom. Wet fractionation is most suitable for this purpose. As liquid oil, preferably low erucic rapeseed, sunflower, saf lower, corn or soyabean oil or a mixture of 2 or more thereof is used. Fully hardening means that the hydrogenation reaction is continued until the reaction is completed as far as is realistically achievable. In practice an iodine value of 0 can rarely be obtained. Preferably, the reaction is continued until the iodine value is less than 3, more preferably less than 2. This means that the hardened fat may still contain a residual amount of unsaturated fatty acids. In a particularly preferred embodiment the fat of the spread has the following N-line: N 10 = 6 - 25% and preferably 8-14% N 20 = 4 - 20% 4-10% N 30 = 0,5 - 8% 0.5-3% N 35 = <3.5% <2%. The fats described in the preceding are not only useful as hardstock materials in fat spreads but equally suited for use as confectionery fats or as a component thereof. In particular the products high in HHM and H 3 are suited for that purpose. In addition these fats are suited as component in so-called bloom inhibitors or anti-blooming agents in confectionery fat mixtures. The invention will hereinafter be explained with the following examples. Parts and percentages refer to weights unless otherwise indicated. EXAMPLES 1 and 2 A hardstock was produced by fully hardening a high lauric rapeseed oil with the following overall fatty acid composition: Fatty acids Overall CIO (Capric) 0.1% C12 (Lauric) 38.8% C14 (Myristic) 4.4% C16 (Palmitic) 3.0% C16:l 0.2% (Palmitoleic) C18 (Stearic) 1.4% C18:l (Oleic) 31.8% C18:2 12.4% (Linoleic) C18:3 6.6% (Linolenic) C20 0.4% (Arachidic) C20:l 0.7% (Eicosenoic) C22 (Behenic) 0.2% The total fatty acid distribution and the fatty acid distribution over the two-position of the fully hardened lauric rapeseed oil is given in the next table: Fatty acids Overall Two-position CIO (Capric) 0.1% — C12 (Lauric) 38.2% 3.4% C14 (Myristic) 4.0% 0.3% C16 (Palmitic) 3.8% 0.8% C18 (Stearic) 52.4% 95.3% C20 1.3% 0.2% (Arachidic) C22 (Behenic) 0.2% - Using the 1, 3-randomness assumption (Coleman, M.H. and Fulton, w.C, 5th Int. Conf. Biochem. Problems of Lipids, Pergamon Press, London (1961)) the following triglyceride composition was determined: Triglyceride group HHH 7.8% HHM 39.1% HMH 0.4% MHM 48.6% HMM 1.9% MMM 2.3% with H: saturated fatty acids with a chain length larger than 15 M: saturated fatty acids with chain lengths 12 and 14 The fully hardened lauric rapeseed oil was used as a margarine hardstock on a level of 8% in sunflower oil (example 1) and 10% in sunflower oil (example 2) . The spreads were processed at laboratory scale through a conventional A-A-C sequence with a throughput of 5.5Kg/hr, an exit temperature on the second A-unit (800 rpm) of 9.7°C, an exit temperature on the C-unit (100 rpm) of 14.5°C. In this processing equipment the A-unit is a scraped surface heat exchanger and the C-unit a crystalliser unit as is well known in the art of margarine and spreads making. 83.3% fat phase were processed with 16% water, 0.6% whey powder and 0.1% potassium sorbate. As a comparative example a margarine was produced according to the above description having a fat phase consisting of 13% of a hardstock obtained by random interesterification of equal amounts of palm kernel fat (m.p. 39°C) and palm fat (m.p. 58°C) , and 87% unhardened sunflower oil. The fatty acid and triglyceride compositions were: Fatty acid Wt% Triglyceride group Wt% C 6 0.1 HHH 19.7 c 8 2.2 HHM 24.0 C 10 2.0 HMH 12.0 C 12 23.7 MHM 7.1 7.6 HMM 14.2 14 MMM 4.2 Cl6 26.1 er " 18.8 C 18 „ 37.0 Oth C 18:l 1.0 C 20 0.3 * C 18 . ! includes both oleic (cis) and elaidic (trans) acid # This group includes triglycerides containing 1 or more fatty acids with a chain length of 10 or less carbon atoms and unsaturated acids. The solid contents, the amounts of saturated fatty acids (SAFA) and the Keys numbers of the three fat phases as well as the physical characteristics of the three produced margarines are given in the next table. The solid contents at 10°, 20°, 30° and 35°C, the N-values, were measured by means of NMR as described in Fette, Seifen, Anstrichmittel 80, (1978), 180-186. The Keys numbers, Kn were calculated according to the formula: Kn = %C12 + %C14 + %C16 + % trans fatty acids - 0.5 * % PUFA. PUFA represents the sum of the percentages of linoleic and linolenic acid. Hardness (Stevens values) and thinness were determined in samples one week after production. All products were virtually free of TRANS fatty acids. Example 1 Example 2 Comparative example Margarine 8 wt% fully 10 wt% fully prepared hardened hardened 13 wt% from lauric lauric interesterified rapeseed oil rapeseed oil hardstock and and 92% and 90% 87 wt% sunflower sunflower sunflower oil oil oil Solids (%) N10 9.2 11.9 12.0 N20 4.8 6.7 7.2 N30 1.0 2.0 3.2 N35 0.3 0.6 0.6 SAFA 19.6% 21.3% 23.8% Kevs -19.5 -18.0 -14.2 Stevens (1 wk) St 5 58 77 86 St 10 51 69 66 St 15 34 50 49 St 20 16 28 26 Thinness (1 wk) 34°C 92 112 156 It is apparent from this table that margarines produced with a low level of non-interesterified, fully hardened hardstock have equal or almost equal hardness values as the margarine produced with a higher level of the interesterified hardstock. Clearly, the fully hardened hardstock contributes more to the hardness per amount of SAFA. The use of the fully hardened hardstocks results in fat blends which contain less SAFA, especially less C16, and therefore contributes more to the cholesterol lowering effect which is expressed by the Keys number. The margarines produced with the non-interesterified, fully hardened hardstock have lower thinness values than the margarine produced with the interesterified hardstock. This resulted in a significantly improved melting behaviour. The consistency of the products remained constant upon temperature cycling and after 4 weeks storage. EXAMPLE 3 The fully hardened lauric rapeseed oil used in examples 1 and 2, was applied as a hardstock at a level of 10% in unhardened sunflower oil. The resulting fat blend was mixed with 65% of a water phase to produce a 35% fat spread. The water phase (65%) contained: 63.1% water 1.3% gelatin 0.5% skimmed milk powder 0.1% P sorbate The spread was processed at laboratory scale through a conventional A-A-A-C sequence with a throughput of 3.7 kg/hr, an exit temperature on the third A-unit (1000 rpm) of 9.0°C, an exit temperature on the C-unit (1000 rpm) of 15.9° C. As a comparative example a 35% spread was produced according to the above description containing a fat phase which consisted of 14% of a hardstock obtained by random interesterification of 57 wt% of a palm kernel fat (m.p. 41°C) and 43 wt% palm fat (m.p. 58°C) , and 86% sunflower oil. The fatty acid and triglyceride composition of the hardstock were: Fatty acid Wt% Triglyceride group wt% - c 6 HHH 16.8 c 8 2.1 HHM 23.3 ^10 2.3 HMH 11.6 c 12 25.9 MHM 7.9 14 8.2 HMM 15.8 5.4 C.6 23.7 MMM # 19.2 C 18 36.0 Other C 18:l 1.3 C 20 0.4 C 2 2 0.1 * Oleic and Elaidic acid # Triglycerides containing short (< C 10 ) or unsaturated acids The solid contents, the amounts of saturated fatty acids (SAFA) and the Keys numbers of the two fat phases as well as the physical characteristics of the two produced 35% fat spreads are given in the next table. The solid contents at 10°, 20°, 30° and 35°C, the N-values, were measured by means of NMR as described in Fette, Seifen, Anstrichmittel 80, (1978), 180-186. Hardness (Stevens values) was determined in samples one week after production. The hardness values show that the product made with the fully hardened hardstock have, especially at lower temperatures, higher hardness values compared to the spread made with the interesterified hardstock. Again, the fully hardened hardstock contributes more to the hardness per amount of SAFA resulting in a reduced use of hardstock and nutritionally more beneficial products. The spreads were tested by a panel of experts. Both products showed a good melting behaviour. The spreadability of the product made with the fully hardened hardstock was found to be superior. Conductivity measurements showed that both products were fat-continuous and remained fat-continuous also after working. Example 3 Comparative example 35% fat 10 wt% fully spread hardened 14 wt% prepared lauric interesterified from rapeseed oil hardstock and and 90% 86 wt% sunflower oil sunflower oil Solids f%) N10 11.9 11.3 N20 6.7 6.5 N30 2.0 3.4 N35 0.6 0.7 SAFA 21.3% 24.7 Kevs -18.0 -13.4 Stevens (1 wk) St 5 56 32 St 10 52 28 St 15 48 27 St 20 26 23 EXAMPLE 4 A hardstock was produced by fully hardening a rapeseed oil which contained 29.5% lauric acid. This resulted in a hardstock with the following overall fatty acid composition and fatty acid composition at the two-position: Fatty acids Overall Two-position CIO (Capric) 0.1% - C12 (Lauric) 29.5% 2.6% C14 (Myristic) 3.5% 0.3% C16 (Palmitic) 3.6% 0.8% C18 (Stearic) 61.6% 96.1% C20 1.4% 0.2% (Arachidic) C22 (Behenic) 0.3% - Using the 1,3-randomness assumption the following triglyceride composition was determined: Triglyceride group HHH 17.9% HHM 47.4% HMH 0.7% MHM 31.1% HMM 1.8% MMM 1.2% with H: saturated fatty acids with a chain length larger than 15 M: saturated fatty acids with chain lengths 12 and 14 According to the procedure described in example 1, the fully hardened rapeseed oil was used as a margarine hardstock on a level of 9% in sunflower oil. The solids content of the resulting fat blend was: N10 10.1% N20 6.2% N30 2.1% N35 1.4% The SAFA content of the fat blend was 20.5% and its Keys number -19.5. In addition this fully hardened rapeseed oil was used as a hardstock on a level of 18% in sunflower oil. The solids content of the resulting fat blend was: N10 19.6% N20 15.7% N30 8.8% N35 3.7% This is an excellent fat blend to produce a shortening. EXAMPLE 5 A hardstock was produced by fully hardening a rapeseed oil which contained 16.1% lauric acid. This resulted in a hardstock with the following overall fatty acid composition and fatty acid composition at the two-position: Fatty acids Overall Two-position CIO (Capric) 0.1% — C12 (Lauric) 16.3% 1.5% C14 (Myristic) 1.8% 0.1% C16 (Palmitic) 4.5% 0.9% C18 (Stearic) 75.3% 97.3% C20 1.6% 0.2% (Arachidic) C22 (Behenic) 0.4% - Using the 1, 3-randomness assumption the following triglyceride composition was determined: Triglyceride group HHH 44.9% HHM 43.0% HMH 0.9% MHM 10.2% HMM 0.9% MMM 0.2% with H: saturated fatty acids with a chain length larger than 15 M: saturated fatty acids with chain lengths 12 and 14 The high level of trisaturated triglycerides with a chain length larger than 15, HHH, makes this hardstock less attractive to apply in a spread since this would result in relatively high N30 and N35 values. And thus in a spread with an unfavourable melting behaviour (high thinness values) . Therefore the hardstock was fractionated. This resulted in an olein fraction (56% yield) with a much reduced HHH content and an strongly increased HHM content. The fatty acid and triglyceride composition of the olein fraction is given in the following table: According to the procedure described in example 1, the fully hardened rapeseed oil was used as a margarine hardstock on a level of 9% in sunflower oil. The solids content of the resulting fat blend was: N10 10.1% N20 7.1% N30 2.6% N35 1.7% The SAFA content of the fat blend was 20.5% and its Keys number -20.1. EXAMPLE 6 The hardstock of example 1 was fractionated using aceton as solvent. The hardstock to aceton weight ratio was 1:4. The fractionation temperature was 26°C. The stearine yield was 44%. Then the stearine fraction was refined using conventional means. The stearine composition was assessed by means of overall and 2-position analysis and carbonnumber measurement: Fatty acids Triglycerides M 3 0.1 MHM 21.3 MMH 1.2 HHM 46.4 HMH 1.5 H 3 29.0 Other 0.5 A margarine fat blend was prepared of 6% of this stearine hardstock and 94% refined sunflower oil. The fat blend had the following properties: N 10 7.8 SAFA 13.6 N 20 4.9 Keys number -21.8 N 30 1.7 N 35 0.9 Margarine was prepared from this fat blend as described in example 1. The product had the following properties: Stevens (after 1 week) at 5°C 48 10°C 43 15°C 30 20°C 19 Thinness 96 (after 1 week) A similar product is prepared except using low erucic rapeseed oil instead of sunflower oil as the liquid oil. The physical properties of the product are very similar, the Keys number is - 9.1, while the SAFA content reduces to 8%.

Claims: CLAIMS Fully hardened, but otherwise not chemically treated fat material having the following fatty acid composition: C 12 9-45wt% C 14 1-5% C 16 3-7% C 18 >40% others up to 10% and preferably up to 5%, these fatty acids being arranged in the following triglyceride combinations: H 3 0-35wt% HHM 20-80% MHM 10-60% M 3 0-10% H representing saturated acids having more than 15 carbon atoms and M saturated acids having 12 or 14 carbon atoms, the sequence of the symbols H and M representing the positon of the fatty acids in the triglyderide molecule. Fat material according to claim 1 wherein the fatty acids are arranged in the following triglyceride combinations: H 3 2-25% HHM 30-80% MHM 10-50% M 3 0-5% A process for producing a fat material usable as a hardstock, said process not involving a blending, or (inter)esterification step, by fully hardening an oil having (a) 9-55 wt% of lauric acid, (b) 20-55% of oleic acid, (c) less than 12 % of saturated C, 4.18 fatty acids and (d) 15 to 35 % of linolenic and linoleic acid; the total of (a) to (d) being more than 90%, and optionally fractionating the fully hardened oil and recovering at least one of the fractions. 4. A process according to claim 3, wherein the oil is derived from brassica seed. 5. A process according to claim 3 or claim 4, the total of (a) to (d) being more than 95%. 6. Hardstock obtainable by a process of claim 3-5. 7. Spread comprising 5-90 % fat phase and 95-10% of an aqueous phase, in which the fat phase comprises 4-20% of a hardstock of claims 1, 2 or 6, the remaining fat being a liquid oil. 8. Spread according to claim 7 wherein the fat phase comprises 8-14% hardstock. 9. Spread according to claims 7-8, having the following N-line N 10 = 6 - 25% and preferably 8-14% N 20 = 4 - 20% 4-10% N 30 = 0,5 - 8% 0.5-3% N 35 = <3.5% <2% 10. Shortening comprising 15-30% of a hardstock of claims 1, 2, or 6 and 85-70% of a liquid oil.

Inventors: SASSEN CORNELIS LAURENTIUS, SASSEN, CORNELIS, LAURENTIUS
Applicants: UNILEVER NV, UNILEVER PLC, UNILEVER N.V.
Application year: 1995
Main classification: A23D9
IPC codes: A23D7, A23D9