• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    method for preparing an edible oil gel, edible oil gel, use of edible oil gel, food product and use of food product. A method of preparing an edible oil gel comprising combining an edible triacyl glycerol oil or triacyl glycerol fat and ethyl cellulose in a weight ratio of 99: 1 to 80:20 to form a mixture, and heat and stir the mixture at a temperature within limits of the range of 80 to 300 ° C to form an oil gel, being carried out the heating and agitation in an inert atmosphere; an oil gel obtainable by said method, its use for preparing food products and products comprising said oil gel.
    公开号:BR112014027719B1
    申请号:R112014027719-2
    申请日:2013-06-06
    公开日:2020-12-15
    发明作者:Roja Ergun；Bradley S. Thomson；David E. Wallick；David M. Meunier
    申请人:Dow Global Technologies Llc；
    IPC主号:
    专利说明:

    [001] The present invention relates to a method for preparing an edible oil gel comprising a fat or oil of triacyl glycerol and ethyl cellulose.
    [002] Structure in solid food products containing fat is provided by the crystalline triacyl-glycerol network. However, these triacyl-glycerols contain high levels of saturated fatty acids. Instead of using naturally very saturated solid fats, oils comprising triacylglycerols having high levels of unsaturated fatty acids are also made into more solid products by hydrogenation or partial hydrogenation. "Trans fats" which are unsaturated fats with a trans isomer inevitably arise from partial hydrogenation of unsaturated oils. Research on the role of oils and fats in human health has indicated that the consumption of saturated fatty acids, even more of trans fatty acids, is associated with high cholesterol levels and cardiovascular diseases.
    [003] Therefore, it is desirable to develop healthier alternatives to saturated or partially hydrogenated fatty acids containing triacyl-glycerols. The demand for a healthy alternative to trans fats and saturated fats creates technological obstacles for the food manufacturing industry. It is difficult to eliminate trans and saturated fats from a food formulation where the goal is to transform a healthier unsaturated oil, which is a liquid at room temperature, into a fat, which is “solid” at room temperature to improve the texture and appearance of a food product.
    [004] In the food industry there have been many attempts to find alternative components that could provide the desired characteristics of texture, structure, stability and flavor that are normally found in hydrogenated oils or vegetable and animal fats. An alternative, organic gels (oil gels), has been recognized for its potential to be used to reduce oil migration in multi-component foods and to act as an alternative to butter or margarine. Oil gels can be used to provide structure for edible oils thereby reducing the need for trans and saturated fatty acids.
    [005] US-B-6,187,323 describes pharmaceutical and cosmetic compositions comprising a mixture of an oil gel and an aqueous gel. In the example, a semi-synthetic triglyceride is gelled with ethyl cellulose in the presence of propylene glycol isostearate by stirring the components at 140 ° C until a uniform oil gel is formed.
    [006] WO 2008/081175 describes compositions containing an active agent for cosmetic and pharmaceutical applications, similar to those of US-B-6,187,323. The compositions are homogeneous mixtures (not emulsions) of a component oil with an aqueous component. In the example, a synthetic oil is gelled with a combination of propylene glycol laurate, ethyl cellulose and propylene glycol isostearate at room temperature before mixing with the aqueous component. The aqueous component is gelled with conventional cosmetic gelling agents.
    [007] In “Influence of the concentration of a gelling agent and the types of surfactant on rheological characteristics of oleogel” (“Influence of the concentration of a gelling agent and types of surfactant on the rheological characteristics of oil gel”) ( I1 farmaco 58 (2003) 1289-1294) MA RuíMartínez et al., Report oil gels comprising olive oil, ethyl cellulose a surfactant selected from OLIVEM 300, 700 and 900. The oil gels were prepared by shaking the components at 100 ° C and are intended for topical use only.
    [008] US-A-4,098,913 describes edible fat particles for incorporation into protein textured meat analog products. Edible fat products are manufactured by gelling a triacyl-glyceride oil or fat with ethyl cellulose. In the example, partially hydrogenated cottonseed oil is mixed with ethyl cellulose under rapid agitation at 180 ° C. Then, the gelled fat is added to the meat analog product. US-A-4,098,913 focuses on a meat substitute having a texture similar to that of meat. The health problem is not addressed and the partially hydrogenated oil used in the example does not prevent the presence of trans fatty acids and is therefore undesirable in terms of health.
    [009] WO 2010/143066 refers to an edible oil gel comprising an oil, ethyl cellulose and a surfactant. It describes that the oil gel is obtained by heating the ethyl cellulose and the surfactant in oil to a temperature above the glass transition temperature of the ethyl cellulose with constant mixing. Appropriately, the mixture is heated to at least 130 ° C to about 160 ° C and after a few minutes a transparent and very viscous solution is formed. Although WO 2010/143066 is not precise about the role of the surfactant and its teaching is contrary to its two priority requests US 61 / 213,480 and US 61 / 213,738 where the surfactant appears to act as a plasticizer. Its presence is mandatory and represents the essence of the described invention.
    [010] However, in many applications, the addition of a surfactant can be avoided, for example, because many surfactants are suspected of causing allergic reactions or other behavioral health problems. Consumers tend to become more and more critical of additives for food products and often prefer a product containing as few unnatural ingredients as possible.
    [011] The problem underlying the present invention is to provide a new method for preparing a solid or semi-solid fat product comprising healthy unsaturated fatty acids and which does not require the addition of a surfactant.
    [012] The problem is solved by a method for preparing an edible oil gel comprising: (I) combining an edible triacyl glycerol oil or triacyl glycerol fat and ethyl cellulose in a weight ratio of 99: 1 to 80 : 20 to form a mixture, and (II) heat and stir the mixture at a temperature within the range of 80 to 300 ° C to form an oil gel, heating and stirring in an inert atmosphere.
    [013] The present invention also relates to the oil gel obtainable by said method, its use for preparing food products comprising said oil gel.
    [014] In the preparation of the oil gel, fat or triacyl glycerol oil are used in a weight ratio of 99: 1 to 80:20, preferably from 95: 5 to 85:15, more preferably from 92: 8 to 87 : 13, and most preferably at a weight ratio of about 90:10.
    [015] Typically, the oil gel comprises from 70 to 99% by weight, preferably from 75 to 95% by weight, more preferably from 80 to 92% by weight and most preferably from 85 to 90% by weight of the fat or oil triacyl-glycerol.
    [016] Triacyl glycerol fat or oil can be a natural, synthetic or semi-synthetic fat or oil such as vegetable or animal fat or vegetable or animal oil, typically triacyl glycerol and a vegetable fat or oil. The term triacyl-glycerol oil means triacyl-glycerols which are liquid at 20 ° C and atmospheric pressure (1013.25 hPa) while triacyl-glycerol fats are solid or semi-solid at 20 ° C and atmospheric pressure (1013.25 hPa) ). The liquid nature of triacyl-glycerol oils is due to their higher content of healthier mono- or polyunsaturated fatty acids, which prevents an arrangement in a crystalline structure. The oil gel of the present invention preferably contains triacyl glycerol oil (s). In preferred embodiments, triacylglycerol fats or oils for use in the present invention have an iodine index of at least 30, more preferably the oil gel contains triacylglycerol oil (s) having an iodine index of at least 70, and in certain incorporations of at least 80. The iodine index is determined according to the official Cd 1-25 method of AOCS (Wijs method).
    [017] Exemplary triacyl-glycerol oils that can be used in the inventive oil gel include canola oil, sunflower oil, corn oil, linseed oil, olive oil, soybean oil, safflower oil (safflower), peanut oil, grape seed oil, sesame oil, argan oil, rice bran oil, seaweed oil, and Echium oil. Exemplary triacylglycerol fats for use in the present invention include cocoa butter and palm oil. Examples of animal oils include squid oil and fish oils such as salmon oil and edible oils from other fish. Mixtures of various fats and triacylglycerol oils (including mixtures of at least two different oils, mixtures of at least two different fats and mixtures of at least one oil and at least one fat), as well as fractions and mixtures of fractions of fats and oils of triacyl-glycerols. In most preferred embodiments, the present oil gel contains canola oil, olive oil, palm oil, cocoa butter, flaxseed oil and sunflower oil.
    [018] Preferably, ethyl cellulose for use in the present invention has a degree of substitution (DS) from 2.40 to 3, preferably from 2.42 to 2.80, more preferably from 2.43 to 2.70, even more preferably from 2.44 to 2.65, even more preferably from 2.45 to 2.60, and most preferably from 2.46 to 2.57. In typical embodiments, ethyl cellulose, including ethyl cellulose having the preferred DS described above, has a viscosity in 5% solution of 3 to 110 mPa-s, preferably 16 to 76 mPa-s, and more preferably of 18 to 50 mPa-s. The term "viscosity in 5% solution" refers to the viscosity of a 5% solution by weight of ethyl cellulose in a mixture of toluene / ethanol in an 80/20 weight ratio. The viscosity at 25 ° C is determined on an Ubbelohde viscometer. A typical viscosimetric analysis is performed as follows: 57 g of a toluene / ethanol mixture is weighed in an 80/20 weight ratio in an 8 ounce dry bottle and 3 g (dry weight) of ethyl cellulose are added. The bottle is placed on a mechanical vibrator and vibrated until all the material forms a solution (approximately 20 min). The resulting solution is analyzed within 24 hours of preparation. To measure viscosity, fill the Ubbelohde viscometer with the solution and then place it in a water bath at 25 ° C until the solution reaches thermal equilibrium at 25 ° C. After the instruction for the Ubbelohde viscometer, the solution is sucked through the calibration tube and then allowed to drain. The flow time between the upper calibration mark and the lower calibration mark is interrupted and the viscosity is calculated according to the instruction taking into account the specific capillary used for measurement.
    [019] The viscosity values in 5% solution reflect the molecular weight of ethyl cellulose.
    [020] Exemplary ethyl celluloses that can be used in the method of the present invention include ETHOCEL ™ Std. 4, ETHOCEL ™ Std. 7, ETHOCEL ™ Std. 10, ETHOCEL ™ Std. 14, ETHOCEL ™ Std. 20, and ETHOCEL ™ Std. 45, all commercially obtainable from The Dow Chemical Company, Midland, USA. ETHOCEL ™ Std. 20 (DS = 2.46 to 2.57, viscosity in 5% solution = 18-22 mPa-s) and ETHOCEL ™ Std. 45 (DS = 2.46 to 2.57, viscosity in solution at 5% = 41-49 mPa-s) are most preferred. Combinations of exemplary ethyl celluloses can also be used.
    [021] In the inventive method, the mixture comprising the fat or oil of triacyl glycerol and ethyl cellulose is heated and stirred, preferably stirred at a temperature within the range of 80 to 300 ° C, preferably from 90 to 250 ° C, typically 130 to 200 ° C, more typically 140 to 170 ° C, even more typically 143 to 160 ° C. Typical warm-up times (holding times) range from 1 to 120 min, preferably from 5 to 100 min, more preferably from 10 to 80 min, even more preferably from 20 to 60 min, and most preferably from 30 to 40 min to if the oil gel forms. Those skilled in the art know that higher temperatures require only short retention times while lower temperatures require longer retention times. In some embodiments, the mixture is heated and stirred at a temperature of 140 to 200 ° C for 20 to 90 min, as well as at a temperature of 145 to 160 ° C for 30 to 60 min. The specific temperature and retention time depends on the type of ethyl cellulose (ie, its molecular weight) and the type of oil or fat. The solubilization stage of ethyl cellulose in triacylglycerol oil / fat is typically determined by touch with visual inspection. If the oil gel has a granular / sandy texture at about 23 ° C, then the ethyl cellulose has not completely dissolved. If the oil gel has a smooth texture at about 23 ° C, ethyl cellulose is considered to be soluble at the processing temperature.
    [022] It is essential for the present invention to perform heating and stirring in an inert atmosphere such as in an atmosphere of inert gas or in ambient air under vacuum (reduced pressure). Examples of inert gases that can be used in accordance with the present invention include nitrogen and noble gases such as, for example, argon. It is preferred to perform heating and stirring in an atmosphere of nitrogen gas. Processing in an inert atmosphere is applied to reduce, preferably minimize and most preferably substantially exclude the presence of oxygen. Typically, the inert atmosphere has an oxygen level of less than 90 g of oxygen / m3, preferably less than 50 g of oxygen / m3, more preferably 30 g of oxygen / m3, even more preferably 25 g of oxygen / m3 and most preferably 23 g of oxygen / m3. The vacuum conditions that can be applied are, for example, underpressures within the range of 70 to 1 kPa, preferably 30 to 2 kPa, and most preferably 10 to 2.5 kPa.
    [023] In the present invention any technique can be applied to create an atmosphere of inert gas including continuously purging the system containing the mixture of oil or fat of triacyl-glycerol and ethyl-cellulose with an inert gas such as nitrogen, for example, with a continuous flow of gas in order to expel air and ensure that air is not reintroduced into the system. It is also possible to evacuate the system to remove air before the inert gas flows into the system. If an inert atmosphere is used, heating and stirring will typically be performed at ambient pressure as well as pressures within the range of 900 to 1100 hPa, preferably 950 to 1060 hPa. However, overpressures of up to 10,500 hPa can be applied.
    [024] In preferred embodiments, the fat or oil of triacyl glycerol and ethyl cellulose are combined by introducing them into the system such as a reactor, for example, a glass reactor. Typically, the mixture is already stirred and the system is purged with inert gas, for example, flowing inert gas such as nitrogen through the system to create an inert atmosphere before heating and the purging of inert gas continues during heating.
    [025] After heating and stirring the mixture in an inert atmosphere at the temperatures described above, the oil gel is preferably cooled, for example, allowed to cool, typically to room temperature, for example, to a temperature less than or equal to 30 ° C or to a temperature less than or equal to 25 ° C or to a temperature less than or equal to 23 ° C or to a temperature less than or equal to 20 ° C. In preferred embodiments, purging of inert gas, that is, the flow of inert gas through the system continues during cooling.
    [026] When the mixture is heated above the glass transition temperature of ethyl cellulose, ethyl cellulose dissolves in the fat or triacyl glycerol oil to create a three-dimensional network of thermoreversible gel in response to cooling. Due to the restricted mobility and migration of the oil / fat within the polymeric network, the present oil gels provide properties such as crystalline triacyl-glycerol solids without the high levels of saturated fatty acids. In many food applications, it is very desirable to replace triacyl-glycerols with healthy oils / fats while retaining structural properties of solid fats.
    [027] It has been observed that very low temperatures and / or insufficient retention times result in an unacceptable sandy texture of the resulting oil gel. This is believed to be due to the unraveling of polymeric ethyl cellulose molecules. Unfortunately, it was further observed that oil / fat comprising unsaturated fatty acids oxidizes easily if kept at elevated temperatures such as at least 80 ° C or 90 ° C, even at least 130 ° C or 140 ° C for times required and quickly become rancid, developing an unpleasant taste and odor. According to the present invention, oil gels are manufactured in an inert atmosphere to prevent oxidation during solubilization. A significant reduction in the level of oxidation is shown in oil gels that are manufactured by the inventive process. No unpleasant taste or odor is detected in various foods when formulated with oil gels prepared according to the present method.
    [028] Although a stabilizer is not required to prepare the oil gel according to the present invention, it can be added in certain embodiments to modify the properties of the oil gel such as increasing its firmness. Examples of stabilizers that can be used in the present method are food-grade emulsifiers and surfactants such as polyoxyethylene sorbitan monooleate (TWEEN 80 or POLYSORBATE 80); polyoxyethylene sorbitan tristearate (TWEEN 65 or POLYSORBATE 65); polyoxyethylene sorbitan monostearate (TWEEN 60 or POLYSORBATE 60); sorbitan monooleate (SMO or SPN 80); sorbitan mono stearate (SMO or SPN 60); glyceryl monooleate (GMO); glyceryl monostearate (GMS); glyceryl monopalmitate (GMP); polyglycerol esters such as polyglyceryl ester of lauric acid - polyglyceryl polyilaurate (PGPL), polyglyceryl ester of stearic acid - polyglyceryl polystearate (PGPS), polyglyceryl ester of oleic acid - polyglycerol polyoleate and polyglycerol polyether polyglyceryl ricinoleate (PGPR); diglycerides; monoglycerides, such as succinylated monoglyceride, lactylated monoglyceride, acetylated monoglyceride, monoglyceride citrate, monoglyceride phosphate, monoglyceride stearyl citrate, and monoglyceride diacetyl tartrate ester; calcium stearoyl lactylate; sodium stearoyl lactylate; sucrose esters; lecithin; and triethyl citrate. If added, the stabilizer is preferably present in an amount that results in a weight ratio of ethyl cellulose / stabilizer less than or equal to 20: 1. The typical ethyl cellulose to stabilizer weight range is 8: 1 to 1: 8, such as, for example, a 5: 1 to 1: 1 ratio.
    [029] In preferred embodiments, the inventive oil gel does not contain any emulsifiers or surfactants other than ethyl cellulose, that is, no emulsifiers or surfactants are added during preparation.
    [030] The oil gel of the present invention may contain additional optional ingredients such as antioxidants to further reduce oxidation. In fact, antioxidants must be food-grade; Exemplary antioxidants for use here include butylated hydroxy-anisol (BHA), butylated hydroxy-toluene (BHT), terciobutyl hydroquinone (TBHQ), ascorbic acid, sodium ascorbate, calcium ascorbate, β-carotene, tocopherols, chlorogenic acids, galates and flavanols. If used, antioxidants are typically added in an amount of up to 10,000 ppm by weight, preferably within the range of 50 to 1000 ppm by weight, and more preferably within the range of 100 to 500 ppm by weight, with based on the total amount of triacyl glycerol oil (s) and fat (s).
    [031] The oil gels of the present invention are edible. They can be formulated into any food product that requires structure fat as solid or semi-solid. Consequently, in a further aspect, the present invention provides a food product comprising an oil gel according to the invention. The food product can be prepared by mixing the food components with an oil gel according to the invention. Mixing can be carried out with the oil gel in a gelled state, or with the oil gel composition in the molten state followed by cooling.
    [032] When used herein, the term "food product" refers to edible products also appropriately containing one or more additional ingredients such as selected from carbohydrates (for example, sugars and starches), proteins, dietary fibers, flavoring agents such as salt, coloring and vitamins. Typically, the food product contains at least about 1% by weight of the oil gel, for example, at least about 5% by weight, at least about 10% by weight or at least about 15% by weight of the gel of Oil. In some embodiments, the food product contains less than 95% by weight of the oil gel, for example, less than about 90% by weight of the oil gel. Examples of food products that can be prepared using the present oil gel include bakery products such as cookies and cakes; bread creams such as margarines and chocolate creams; chocolate and fillings.
    [033] In certain embodiments, the food product according to the present invention is a meat product. For example, a ground beef product such as hamburger meat, or a meat emulsion product such as sausage, bologna, sausages, or other sausage-like products. Typically, the meat products of the invention comprise 10 to 25% by weight of protein, 5 to 35% by weight of fat (including oils and oil gels), and 40 to 60% by weight of total water. Replacing a fraction of the animal fat present in such products with oils, appropriately vegetable oils, results in meat products having an unacceptably hard, chewy and / or viscous texture when cooked. However, it has been found that replacing a fraction of animal fat with an oil gel according to the present invention results in meat products that do not exhibit these defects.
    [034] Some embodiments of the invention will now be described in detail in the following examples in which all parts and percentages are given by weight unless otherwise specified. Examples Raw materials
    Example 1
    [035] 75 g of ethyl cellulose (ETHOCEL ™ Std. 20) and 675 g of canola oil were weighed and placed in a glass reactor. During the stirring of ethyl cellulose and oil, nitrogen flowed through the reactor to remove air and create a nitrogen environment (oxygen level less than 23 g / m3) before heating. The mixture was heated to 150 ° C while stirring at 200 rpm and maintained at that temperature for 60 min with continuous stirring. At the end of the retention time, the resulting solution was allowed to cool to an ambient temperature of about 25 ° C. Nitrogen flowed through the reactor during the heating and cooling process to ensure that oxygen was not introduced into the system. Comparative Example 2
    [036] In Comparative Example 2, the procedure of Example 1 was followed except that it was carried out in air, that is, no nitrogen flowed through the reactor. Examples / Comparative Examples 3 to 15
    [037] In these examples, the procedure of Example 1 / Comparative Example 2 was followed, except that ETHOCEL ™ Std. 45 was used instead of ETHOCEL ™ Std. 20 and the heating temperature was 160 ° C for a retention time 40 min. Different oils were used instead of canola oil reported in the table below. In Comparative Example 4 and Example 6, tocopherol was added to the reactor during heating (at about 63 ° C) as an antioxidant in an amount of 0.135 g to 750 g of the mixture of ETHOCEL ™ Std. 45 and oil.
    [038] Example 7 was prepared under vacuum conditions by pulling a vacuum (15 inches Hg) from the glass reactor during stirring and before heating. After 5 min of stirring under vacuum, the mixture was heated to 160 ° C and the target temperature was maintained for 40 min. When the reactor was allowed to cool, the vacuum was removed at about 80 ° C and the reactor was rendered inert with nitrogen. Test results and discussion Free space gas chromatography - Volatiles
    [039] Free space GC / FID and GC / MS were used to identify and monitor volatile levels in Example 1 and Comparative Example 2.
    [040] Figure 1 is a GC / MS chromatogram of a 10/90 (w / w) mixture of ETHOCEL ™ Std. 20 and canola oil after heating to 150 ° C in a small sealed space bottle for 60 min .
    [041] Various aldehydes and alcohols (volatiles) have been identified as oil decomposition products as follows: (a) hexanal; (b) 1-pentenol; (c) heptanal; (d) hexenal; (e) pentanol; (f) heptenal; (g) nonanal; (h) 2-octenal; (i) 1-octen-3-ol; (j) + (k) heptadienal; (l) decennial.
    [042] Many of the compounds identified are recognized as oxidizing products of vegetable oils and are often associated with odor and taste.
    [043] Figure 2 is a GC-FID chromatogram of Comparative Example 2.
    [044] Figure 3 is a GC-FID chromatogram of Example 1.
    [045] Observation of the figures makes it evident that volatile levels have been dramatically affected by the presence of air. For Example 1 according to the present invention and carried out in an inert environment (nitrogen) the levels of volatiles were 10-25 times lower than with an air environment (Comparative Example 2). Peroxide and p-anisidine values
    [046] The oxidation process can be divided into two stages: in the first stage of oxidation, fatty acids react with oxygen to form odorless products such as peroxides while in the second stage the peroxides degrade into various substances that are responsible for the smell and rancid odor. The peroxide value test (PV) can be used to determine the primary oxidation products while the p-anisidine test can be used to measure the secondary products. The last method determines the amount of aldehydes (mainly 2-alkenals and 2,4-dienals) by reaction in an acetic solution of aldehydes and p-anisidine. The PV and the p-anisidine (p-AV) value can be combined to assess the level of oxidation of oil samples: with PV you can determine the oxidative status of the product while with p-AV you can determine the oxidative history of the product.
    [047] Peroxide and p-anisidine values from Examples / Comparative Examples 3 to 15 have been determined and p-anisidine values are reported in the table below. Peroxide values were determined using the acetic acid / chloroform method according to the official AOCS Cd 8-53 method, revised in 1990 and updated in 1992. By convention, the p-AV value is defined as 100 times the density optics measured at 350 nm in a 1 cm cell of a solution containing 1.00 g of oil / fat in 100 ml of chloroform mixture and a solution of p-anisidine in glacial acetic acid according to the official method Cd 18-90 of AOCS (the official method Cd 18-90 of AOCS uses isoctane while here chloroform is used because it is a good solvent for ethyl cellulose. The peroxide values of the samples prepared in both air and nitrogen environments were close The low peroxide values suggest that the primary oxidation levels of the products were very low regardless of the environment in which they were prepared.
    [048] The p-anisidine values of all samples suggest some level of oxidative history in the samples. For most examples, the p-anisidine values of inventive oil gels prepared in a nitrogen environment (Examples 5, 6, 7, 9 and 11) were at least 50% lower than those prepared in an air environment (Comparative Examples 3, 4, 8, and 10); for Examples 13 and 15 the p-anisidine values of the inventive oil gels were about 43 and 38% lower than those prepared in an air environment (Comparative Examples 12 and 14). These results show that the method according to the present invention significantly decreases oxidation.
    权利要求:
    Claims (12)
    [0001]
    1. Method for preparing an edible oil gel, characterized by the fact that it comprises: - combining an edible triacyl-glycerol oil or triacyl-glycerol fat and ethyl cellulose in a weight ratio of 99: 1 to 80:20 to form a mixture, and - heat and stir the mixture at a temperature within the range of 140 ° C to 200 ° C for 20 to 90 minutes to form an oil gel, with triacyl glycerol oil or triacyl glycerol fat edible has an iodine value of at least 30, determined according to the official AOCS Cd-125 method (Wijs method) and heating and stirring is carried out under an inert atmosphere, the said method being free of surfactants; and - cool the oil gel to a temperature below 30 ° C, the cooling being conducted in an inert atmosphere.
    [0002]
    2. Method according to claim 1, characterized in that the inert atmosphere is an atmosphere of inert gas, preferably an atmosphere of nitrogen gas or noble gas.
    [0003]
    Method according to either of claims 1 or 2, characterized in that the heating and stirring are carried out in an inert atmosphere containing less than 90 g / m3 of oxygen.
    [0004]
    Method according to any one of claims 1 to 3, characterized in that the ethyl cellulose has a degree of substitution from 2.40 to 3.00, preferably from 2.45 to 2.60.
    [0005]
    Method according to any one of claims 1 to 4, characterized in that the ethyl cellulose has a viscosity in 5% solution of 3 to 110 mPa-s, preferably of 16 to 76 mPa-s, measured as a 5% by weight solution of ethyl cellulose in an 80/20 (w / w) mixture of toluene / ethanol at 25 ° C in an Ubbelohde viscometer.
    [0006]
    Method according to any one of claims 1 to 5, characterized in that the edible triacyl-glycerol oil or triacyl-glycerol fat is of natural origin.
    [0007]
    Method according to any one of claims 1 to 6, characterized in that the edible triacyl glycerol oil is selected from canola oil, sunflower oil, corn oil, linseed oil, palm oil, olive oil, soy oil, safflower oil (safflower), peanut oil, grape seed oil, sesame oil, argan oil, rice bran oil, seaweed oil, Echium oil, squid oil , salmon oil, edible fish oil, fractions and mixtures thereof.
    [0008]
    Method according to any one of claims 1 to 7, characterized in that the mixture is heated and stirred at a temperature of 145 to 160 ° C for 30 to 60 min.
    [0009]
    9. Edible oil gel, obtained by the method defined in any one of claims 1 to 8, said oil gel being characterized by the fact that the mixture is heated and stirred at a temperature of 145 to 160 ° C for 30 to 60 minutes and the oil gel is free of any emulsifier or surfactant in addition to ethyl cellulose and the edible triacyl glycerol oil is selected from canola oil, sunflower oil, corn oil, flax oil, palm oil , olive oil, soy oil, safflower oil (safflower), peanut oil, grape seed oil, sesame oil, argan oil, rice bran oil, seaweed oil, Echium oil, squid, salmon oil, edible fish oil, fractions and mixtures thereof.
    [0010]
    10. Use of edible oil gel, as defined in claim 9, characterized by the fact that it is for preparing a food product.
    [0011]
    11. Use according to claim 10, characterized in that the oil gel replaces at least part of a solid or semi-solid fat in the food product.
    [0012]
    12. Use according to either of claims 10 or 11, characterized in that the food product is selected from bakery products such as cookies and cakes; bread creams such as margarines and chocolate creams; chocolate and fillings.
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    法律状态:
    2018-03-06| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2018-03-13| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2018-03-20| B06I| Publication of requirement cancelled [chapter 6.9 patent gazette]|Free format text: ANULADA A PUBLICACAO CODIGO 6.6.1 NA RPI NO 2462 DE 13/03/2018 POR TER SIDO INDEVIDA. |
    2018-03-27| B15K| Others concerning applications: alteration of classification|Ipc: A23D 9/02 (2006.01), A23D 7/015 (2006.01), A21D 13 |
    2019-07-30| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|
    2020-03-24| B06A| Patent application procedure suspended [chapter 6.1 patent gazette]|
    2020-09-01| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|
    2020-12-15| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 06/06/2013, OBSERVADAS AS CONDICOES LEGAIS. |
    2021-07-13| B25A| Requested transfer of rights approved|Owner name: THE DOW CHEMICAL COMPANY (US) |
    2021-07-27| B25A| Requested transfer of rights approved|Owner name: DDP SPECIALTY ELECTRONIC MATERIALS US, INC. (US) |
    2021-08-10| B25D| Requested change of name of applicant approved|Owner name: DDP SPECIALTY ELECTRONIC MATERIALS US, LLC (US) |
    2021-08-24| B25A| Requested transfer of rights approved|Owner name: NUTRITION AND BIOSCIENCES USA 1, LLC (US) |
    优先权:
    申请号 | 申请日 | 专利标题
    US201261665444P| true| 2012-06-28|2012-06-28|
    US61/665,444|2012-06-28|
    US201261670908P| true| 2012-07-12|2012-07-12|
    US61/670,908|2012-07-12|
    PCT/US2013/044461|WO2014004018A1|2012-06-28|2013-06-06|Method of preparing an edible oleogel|
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