process for modifying the characteristics of citrus fiber, citrus fiber, blend of citrus fiber, a pr

专利摘要:
process for modifying the properties of citrus fiber. The present invention relates to the process for modifying citrus fiber. Citrus fiber is obtained having a packaging concentration value close to c * of less than 3.8 wt.%, anhydrous base. the citrus fiber may have a viscosity of at least 1000 mpa.s, wherein said citrus fiber is dispersed in standardized water at a mixing speed of between 800 rpm to 1000 rpm, to a standardized 3% citrus fiber / water solution by weight, and wherein said viscosity is measured at a shear rate of 5s ^ -1 ^ at 20 <198> c. Citrus fiber may be obtained having a lipid value of at least 90. Citrus fiber may be used in food products, food products, beverages, personal care products, pharmaceuticals or debris products.
公开号:BR112013002320B1
申请号:R112013002320
申请日:2011-07-29
公开日:2018-10-16
发明作者:Hiram Reeder David；Andre Christian Mazoyer Jacques；René Pierre Wallecan Joël；Walter Gusek Todd
申请人:Cargill Inc；
IPC主号:

专利说明:

(54) Title: PROCESS TO MODIFY THE CHARACTERISTICS OF CITRUS FIBER, CITRUS FIBER, CITRUS FIBER MIXTURE, A PRODUCT UNDERSTANDING A CITRUS FIBER OR MIXTURE AND USE OF A CITRUS FIBER (51) lnt.CI .: A23L 33/10; A23L 19/00; A23L 33/00; A23L 29/00; A23L 33/21 (30) Unionist Priority: 10/08/2010 EP 10008316.1, 07/30/2010 US 61 / 369,207 (73) Holder (s): CARGILL, INCORPORATED (72) Inventor (s): TODD WALTER GUSEK; JACQUES ANDRE CHRISTIAN MAZOYER; DAVID HIRAM REEDER; JOÉL RENÉ PIERRE WALLECAN (85) National Phase Start Date: 30/01/2013
1/19
Invention Patent Description Report for PROCESS TO MODIFY THE CHARACTERISTICS OF CITRUS FIBER, CITRUS FIBER, CITRUS FIBER MIXTURE, A PRODUCT UNDERSTANDING A CITRUS FIBER OR MIXTURE AND USE OF A CITRUS FIBER.
CROSS REFERENCE FOR RELATED ORDERS
This application claims the benefit of United States Provisional Patent Application No. 61 / 369,207, filed on July 30, 2010 entitled PROCESS TO MODIFY CITRUS FIBER PROPERTIES and European Patent Application No. 10008316.1, filed on August 10, 2010 entitled PROCESS TO MODIFY CITRUS FIBER PROPERTIES, which are incorporated herein by reference in their entirety. TECHNICAL FIELD
The present invention relates to a process for modifying the properties of citrus fiber. The resulting dry citric fiber is useful as a food additive in food products, products intended for animal feed and drinks. Citric fiber is also useful in personal care, pharmaceutical or detergent products.
BACKGROUND OF THE INVENTION
The prior art describes processes for extracting citrus fiber.
For example, U.S. Patent No. 7,094,317 (Fiberstar, Inc.) describes a process for refining cellulosic material from organic fiber plant mass (such as citrus). The process describes a first step of immersing the organic fiber plant mass in an aqueous solution, draining the organic fiber plant mass and allowing it to sit long enough to allow cells in the organic fiber plant mass to open cells and expand the mass of organic fiber plant. The immersion step requires at least 4 hours and is reported to be critical in order to get the materials to completely soften. The immersed raw material is then refined under high depth and dried.
W.O. Patent Application No. 94/27451 (The Procter & Gamble
Company) describes a process for producing a citrus pulp fiber, in which a first aqueous suspension of citrus pulp is prepared which is then heated to a temperature of 700 to 1800 for at least
Petition 870180062802, of 07/20/2018, p. 7/15
2/19 minus 2 minutes. The suspension is then subjected to a high shear treatment.
W.O. Patent Application No. 2006/033697 (Cargill, Inc.) describes a process of extracting citric fiber from citrus vesicles. The process includes washing citrus vesicles with water, contacting water-washed vesicles with an organic solvent to obtain vesicles washed by organic solvent, removing solvents from the vesicles washed by organic solvent and recovering dry citric fiber from it.
While the prior art reports that citrus fiber with useful properties is obtained, there remains a need to also improve the characteristics of citrus fiber.
Consequently, it is an object of the present invention to develop a process for modifying the properties of citrus fiber. It is also an objective of the present invention to obtain citric fiber which has good hydration ability and viscosity properties.
SUMMARY OF THE INVENTION
The present invention, according to one aspect, is directed to a process for modifying the properties of citrus fiber. In one embodiment, citric fiber is hydrated and treated to obtain homogenized citric fiber. The process also comprises a step of washing the homogenized citric fiber with an organic solvent to obtain citric fiber washed by organic solvent. The citric fiber washed by organic solvent is removed from the solvent and dried, and modified citric fiber is recovered.
In another aspect of the present invention, citric fiber is obtained by the process of the present invention. Citric fiber has a packaging concentration close to less than 3.8% w / w, anhydrous base. In a preferred embodiment, the citrus fiber has a viscosity of at least 1000 mPa.s, wherein said citrus fiber is dispersed in standardized water at a mixing speed of between 800 rpm to 1000 rpm, preferably 900 rpm, to a solution of citric fiber / standardized water at 3% w / w, and in which the said temperature is measured at a shear rate of 5 s' ¹ at 20 ° C. In another preferred embodiment, the citric fiber has a
3/19 CIELAB L * of at least 90.
In yet another aspect, the present invention is directed to a mixture of citrus fiber of the present invention and plant-derived fiber (for example, derived from cereals).
In yet another aspect, the present invention is directed to a food product, a food product, a beverage, a personal care product, a pharmaceutical product or a detergent product comprising the citrus fiber according to the present invention.
In yet another aspect, the present invention is directed to the use of citrus fiber as a texturizer or viscosifier in food products, food products, beverages, personal care products, pharmaceuticals or detergents.
BRIEF DESCRIPTION OF THE DRAWINGS.
Figure 1 is a schematic illustration of a process according to a preferred embodiment of the present invention.
Figures 2a and 2b are an illustration according to a test method used in the present application.
DETAILED DESCRIPTION OF THE INVENTION
In one aspect, the present invention is directed to a process for modifying the properties of citrus fiber.
The term citrus fiber, when used herein, refers to a component of fibrous pecto-cellulosic obtained from citrus pulp, citrus peel, citrus pieces and combinations thereof.
The process according to the present invention can be used to modify the citrus fiber properties obtained from a wide variety of citrus fruits, non-limiting examples of which include oranges, tangerines, limes, lemons, and grapefruit. In a preferred embodiment, citrus fiber is orange fiber.
In the process according to the present invention, citrus fiber which is typically in a dry form, is first hydrated, preferably with water.-Q. Preferably, the citrus fiber is hydrated with water at a dry matter content of 5% w / w or less. Hydrated citric fiber is
4/19 then treated to obtain homogenized citric fiber. Homogenization can be carried out by several possible methods including, but not limited to, high shear treatment, pressure homogenization, colloidal grinding, intensive mixing, extrusion, ultrasonic treatment, and combinations thereof. Preferably, the energy input (energy per unit volume) to perform homogenization is at least 1000 kW per cm ³ of citric fiber.
In a preferred embodiment of the present invention, the homogenization treatment is a pressure homogenization treatment. Pressure homogenizers typically comprise an alternative plunger or piston pump together with a homogenization valve assembly attached to the discharge end of the homogenizer. Suitable high pressure homogenizers include high pressure homogenizers manufactured by GEA Niro Soavi, from Parma (Italy), such as the NS Series, or the homogenizers from Gaulin and Rannie series manufactured by APV Corporation of Everett; Massachusetts (US).
During pressure homogenization, the citric fiber is subjected to high shear rates as a result of cavitation and turbulence effects. These effects are created by the citrus fiber entering the homogenization valve assembly from the pump section of the homogenizer at a high pressure (and low speed). Suitable pressures for the process of the present invention are from 5 MPa to 100 MPa (50 bar to 1000 bar).
Depending on the particular pressure selected for the pressure homogenization, and the flow rate of the citric fiber through the homogenizer, the citric fiber can be homogenized by one step through the homogenizer. However, more than one step of the citrus fiber may be required.
In one embodiment, the citric fiber is homogenized by a Cynic pass through the homogenizer. In a single homogenization step, the pressure used is preferably 30 MPa to 100 MPa (300 bar to 1000 bar), more preferably 40 MPa to 80 MPa (400 bar to 800 bar),
5/19 even more preferably from 50 MPa to 75 MPa (500 bar to 750 bar).
In another preferred embodiment, the citric fiber is homogenized by multiple steps through the homogenizer, preferably at least 2 steps, more preferably at least 3 steps through the homogenizer. In a multistep homogenization, the pressure used is typically lower compared to a single-step homogenization and preferably from 10 MPa to 60 MPa (100 bar to 600 bar), more preferably from 20 MPa to 50 MPa (200 bar to 500 bar) bar), even more preferably from 30 MPa to 40 MPa (300 bar to 400 bar).
Optionally, the citric fiber can be subjected to a heat treatment before homogenization. Preferably, the temperature used in the heat treatment can vary from 50 ° C to 140 ° C over a period of 1 second to 3 minutes. Heat treatment can be used for pasteurization of citrus fiber. For pasteurization, the heat treatment preferably employs a temperature between 65 ° C to 140 ° C, preferably from 80 ° C to 100 ° C for a period between 2 seconds to 60 seconds, preferably from 20 seconds to 45 seconds. Pasteurization is preferred over inactive pectinesterases to prevent loss of turbidity and to inactivate waste microorganisms to enhance storage stability.
The homogenized citric fiber is then contacted with an organic solvent. In one aspect, extracts of organic solvent, water, flavors, odors, colors and the like of citrus fiber. The solvent should preferably be polar and water miscible to better facilitate removal of the desired components. Available solvents can include lower alcohols such as methanol, ethanol, propanol, isopropanol, or butanol. Ethanol and isopropanol are preferred solvents. The solvent can be supplied in an aqueous solution. The concentration of solvent in the solvent solution most often ranges from about 70% by weight to about 100% by weight. In one embodiment, a 75% by weight aqueous ethanol solution is used as the solvent. In a preferred embodiment, a .90% aqueous ethanol solution. by weight is used as a solvent. In general, solvents will remove water-soluble components at lower concentrations and components
6/19 oil soluble in higher concentrations. Optionally, a more non-polar co-solvent can be added to the aqueous alcohol to improve the recovery of oil-soluble components in the citric fiber. Examples of such non-polar solvents include ethyl acetate, methyl ethyl ketone, acetone, hexane, methyl isobutyl ketone and toluene. The most non-polar solvents can be added to up to 20% of the solvent mixture. Many solvents, such as ethanol, have a lower heat of vaporization than water, and therefore require less energy to volatilize than would be required to volatilize an equivalent mass of water. The solvent is preferably removed and reformed for reuse.
Preferably, the citrus fiber is contacted with organic solvent in a solids-to-solvent weight ratio of at least about 0.25: 1, preferably at least about 0.5: 1, and often at least about 0.75: 1 , from about 1: 1 to about 5: 1, or from about 1.5: 1 to about 3: 1, based on the wet weight of the solids. In one embodiment, the solids-to-solvent ratio is about 2.Ί.
Extraction can be performed using a single stage but preferably it can be performed using multi-stage extraction, for example, a two-, three-, or four-stage extraction process, and preferably using counter-current extraction. There is no particular upper limit for the number of extraction stages that can be used. Figure 1 schematically illustrates a preferred embodiment in which a two-stage countercurrent extraction process employs first and second solvent extractors 25a and 25b, respectively.
After homogenization 10, homogenized citric fiber is fed into the second extractor 25b. An aqueous ethanol solvent is fed from a solvent tank 26 into the first solvent extractor 25a. Spent solvent from the first solvent extractor 25a is fed into the second solvent extractor 25b, while the citrus fiber from the second solvent extractor 25b is fed into the first solvent extractor 25a. Spent solvent from the second solvent extractor 25b can be fed to an evaporator 35 (optional) to separate solids (eg, sugars,
7/19 acids, colors, flavors, citrus oils, etc.) from the spent solvent, which can be condensed and returned to a further 24. Distillations (predominantly water) are separated and removed.
After each stage of extraction, liquid is preferably also removed. A suitable device is a centrifugal decanter. Alternatively, a sieve, belt filter press or other suitable device for removing liquids can be used.
Citric fiber from the first solvent extractor 25a is fed into a solvent remover 30. The solvent remover 30 removes solvent and water from the solids that remain after extraction, allowing the solvent to be reformed for future use and in the same way ensuring that the product is safe for grinding and commercial use. The solvent remover 30 may employ indirect heat to remove significant amounts of solvent from the solid residue. Alternatively, direct heat can be provided to dry, for example, by providing hot air from flash dryers or fluidised flow dryers. Direct steam can be used, if desired, to remove any trace amounts of solvent remaining in the solids. Vapors from solvent remover 30 are preferably recovered and fed to the still 24 to recycle at least a portion of the solvent.
Retention time at each extraction step can vary over a wide range but can be about 5 minutes or less per extraction step. The temperature in the solvent extractor (s) depends on such factors as the type of solvent used but most often ranges from about 4 ° C to about 85 ° C at atmospheric pressure. Temperatures can be suitably increased or decreased for operation under super or sub-atmospheric pressures. Optionally, techniques such as ultrasound are used to enhance the efficiency of the extraction process. By keeping a closed system, solvent losses during extraction, removal of solvents, and distillation can be minimized. Preferably, at least about .____ 70% by weight of. solvent is recovered and reused. A solvent preparation stream releases fresh solvent into the solvent tank 26 to
8/19 replenish any solvent that is not recovered.
In a preferred embodiment, the process according to the present invention also comprises a fragmentation or spraying step before removing the solvent and drying. Suitable methods include, but are not limited to, grinding, milling, crushing, high speed mixing, or impact. Fragmentation or spraying can be beneficial to disintegrate any agglomerations or aggregates that are left after removing liquid with the belt filter pressing step. This step further facilitates solvent removal. While not wishing to be bound by theory, it is believed that fragmentation or spraying also opens up the fibers. As a result of this, the solvent is more evenly distributed and easier to remove in the subsequent solvent removal and drying step. In yet another preferred embodiment, the fragmentation or spraying step is used in combination with added and dispersed water or a mixture of water and a solvent (as described above) to enhance solvent removal and drying and achieve the desired moisture in the fiber. citrus finally obtained for a particular purpose use.
In another preferred embodiment, the process according to the present invention also comprises a fragmentation or spraying step after drying. This fragmentation or spraying post drying step can be performed to also reduce the particle size of the citrus fiber, to improve fluidity, dispersibility, and / or hydration properties.
In yet another preferred embodiment, the process according to the present invention also comprises the step of subjecting the citrus fiber to a processing aid. Preferably, processing aid is selected from the group consisting of enzymes, acids, bases, hydrocolloids, vegetable fiber, bleaching agent, and combinations thereof. Preferably, the processing aid is mixed with the citrus fiber before homogenization. --------- In one aspect of the present invention, process aid can
9/19 be used to sew the properties of the finally obtained citric fiber.
Preferred enzymes include, but are not limited to, pectinase, protease, cellulase, hemicellulase and mixtures thereof. When enzymes are used, they will be used before any heat treatment that inactivates them, and preferably in the same way before homogenization. Inactivation by heat treatment is however desired once the desired effect is obtained.
Preferred acids include, but are not limited to, citric acid, nitric acid, oxalic acid, ethyldiodiaminatetraacetic acid and combinations thereof. Citric acid is however more preferred when it is a food grade acid.
A preferred base is caustic soda.
Preferred hydrocolloids include, but are not limited to, pectin, alginate, locust bean gum, xanthan gum, guar gum, carboxymethylcellulose and combinations thereof.
A bleaching agent can also enhance the color properties (ie it makes the citrus fiber even whiter). A preferred bleaching agent is hydrogen peroxide.
The citrus fiber obtained by the process according to the present invention has improved properties over other citrus fibers of the prior art. Especially, the citric fiber has good swelling behavior, hydration capacity and viscosification properties. It is capable of building viscosity under relatively low shear.
The citric fiber of the present invention has a packaging concentration close to less than 3.8% by weight, anhydrous base. Preferably, the packaging concentration close to c * is less than 3.6, even more preferably less than 3.4, and preferably less than 3.2% by weight, anhydrous base. The determination of the packaging concentration close to c * is described here in the test method section below. With the process of the present invention, the value of c * can be decreased by at least 5%, and often by at least 10% and even more than 20%. Even with a difference of 5%, the properties of the fiber are significantly different.
The citric fiber has a moisture content of 5% to 15%, more preferably 6% to 14%, preferably. Preferably, at least 90% of the particle volume has a diameter of less than 1000 microns, preferably from 50 micrometers to 1000 micrometers, more preferably from 50 micrometers to 500 micrometers, even more preferably from 50 micrometers to 250 micrometers.
The citric fiber preferably has a viscosity of at least 1000 mPa.s, wherein said citric fiber is dispersed in standardized water at a mixing speed of between 800 rpm to 1000 rpm, preferably 900 rpm, to a solution of fribra water citrate / standardized at 3% w / w, and in which said viscosity is measured at a shear rate of 5 s' ¹ at 20 ° C. Preferably, the viscosity at a shear rate of 5 s' ¹ at 20 ° C is at least 2000 mPa.s, more preferably at least 3000 mPa.s, even more preferably at least 4000
-7-mPa.s, even more preferably at least 5000 mPa.s was still 15000 mPa.s. The preparation of standardized water, and the method for measuring viscosity is described in the test method section here below.
With the process of the present invention, the viscosity of the citric fiber is typically increased (measured under the above conditions) by at least 100%. In some modalities, it is even increased by at least 200%. It is even possible in some embodiments to increase viscosity by more than 1000%.
The citrus fiber according to the present invention has good emulsification properties, as shown in the examples. The D4.3 value in the oil-rich phase is typically below 15 micrometers for the citric fiber of the present invention.
The citric fiber of the present invention can likewise have excellent whiteness properties, even without the need to use bleaching agents. Citric fiber typically has a CIELAB L * value of at least 85. However, with the process at odds with the present invention, it is possible to obtain much higher L * values. In this way,
11/19 According to another aspect, the present invention is directed to a citrus fiber having a CIELAB L * of at least 90, preferably at least 92, even more preferably at least 93. Preferably, the citrus fiber has a value of CIELAB b * less than 20, even more preferably less than 15. The method for determining CIELAB L * and b * values is described in the test method section here below. As discussed above, bleaching agents can also be used as processing aids in the process to also improve the whiteness of the citrus fiber.
The citrus fiber according to the present invention can be mixed with other fibers, such as fibers derived from plants (for example, vegetables, grains / cereals), with other citrus fibers such as citrus fiber obtained from citrus peel or citrus pieces, or combinations thereof. The mixture can be in dry or liquid form.
In another aspect, the citrus fiber of the present invention and the mixtures described can be used here previously in food applications, food applications, beverages, personal careless products, pharmaceutical products or detergent products. The amount of citrus fiber (or mixture) to be used depends on the particular application and the desired benefit to be obtained, and is within the knowledge of a knowledgeable person.
Food applications may include, but are not limited to, dairy products, frozen products, bakery products, fats and oils, fruit products, confectionery, meat products, soups, sauces and seasonings. Dairy products include, but are not limited to, yogurt, fresh cheese, quark, processed cheese, dairy desserts, mousses. Frozen products include, but are not limited to, ice cream, sorbet, water ice. Bakery products include, but are not limited to, cakes, pastry goods, dough, patisserie, extruded snacks, fried snacks. Fats and oils include, but are not limited to, margarines, low-fat expansions, cooking fats. Fruit products include, but are not limited to, .fruit preparations, yogurt fruit preparations, preserves, jams, jellies. Confectionery includes, but is not
12/19 limited to, sweet, chocolate expansions, nut based expansions. Meat products include, but are not limited to, chilled or frozen processed and poultry meat, preserved meat products, fresh sausage, cured sausage and salami.
Drinks can include concentrates, gels, energy drinks, carbonated drinks, non-carbonated drinks, syrups. The drink can be any medical syrup or any drinkable solution including iced tea, and fruit juices, vegetable-based juices, lemonades, cordial, nut-based drinks, cocoa-based drinks, dairy products such as milk , whey, yogurts, buttermilk and drinks based on it. Beverage concentrates refer to a concentrate that is in a liquid form.
Personal care products can include cosmetic formulations, hair care products such as shampoos, conditioners, creams, styling gels, personal wash compositions, sun creams and the like.
Detergent products can include hard surface cleaners, fabric cleaners or conditioners, and the like. Testing methods
1. Standardized water preparation
Dissolve 10, Og of NaCI and 1.55g CaCl2.2H ₂ O in low conductivity water (for example milli-Q Ultrapure Millipore 8.2 MQcm), and prepare 1 liter to prepare standard water raw material.
Use a 100ml aliquot of the standard water raw material and prepare 1 liter with low conductivity water.
2. Measure packaging concentration close to C *
2.1 Principle
Samples of citric fiber (n> 10) are humidified with ethylene glycol, dispersed in standard tap water, and subjected to an MCR301-controlled shear stress oscillatory test (CSS). Citric fiber dispersions are measured in increments of .25% w / w in the range of 1.75 - 5.00% w / w. The linear viscoelastic band (LVR) moduli complex G * is
13/19 plotted against concentration. The packaging concentration close to c * is determined by two methods of crossing tangents on a linear scale.
2.2 Apparatus
- Anton Paar MCR301 rheometer with coaxial cylinder configuration (TEZ150P-CF Peltier at 20 ° C) with ST24-2D / 2V / 2V3D wind vane probe, measuring cup with CC27 / T200 / SS / P grooves and water bath circulating cooling fixed at 15 ° C. The kit must be clean and dry, and the MCR301 units must be turned over 30 minutes before use. Checks should be made according to the supplier's instruction manual (see instruction manual). The pump and circulating bath should be in use at all times to avoid burning the Peltier unit. According to the manufacturer, the water bath must be loaded with demineralised water containing a maximum of 30% antifreeze (for example ethylene glycol).
- RWD 20 Digital IKA agitator and lower paddle (4 paddle propeller
410 00) u-;
- 600 ml Duran glass beaker (01Ocm)
- Laboratory balance having an accuracy of 0.01 g
- Hard plastic soup spoon
2.3 Procedure
Start System
Start the circulating bath (loaded with demineralized water + 30% ethylene glycol (eg Merck 1.00949.1000, CAS [107-21 -1])) and then the rheometer according to the procedure explained in the instruction manual. Select the folder and perform the initialization procedure according to the instruction manual.
System calibration
The standard calibration check procedure for the MCR301 is fully described in the instruction manual and should be performed in accordance with the instruction manual. MCR301 instruments must be ready (started and all parameters checked) before testing citrus fiber dispersions. The ST24 CSR measurement system
14/19 should be set to 1 and the CSS value (Pa / mNm) should be set with certified Newtonian oil calibration (eg Cannon N100, available from Cannon Instrument Company, State College, PA 16803, USA).
Sample preparation
- Place a 600 ml glass beaker in the laboratory balance, and zero the balance.
- Weigh in the beaker the required grams (x) of citric fiber, to the nearest 0.01 g, according to the moisture content (m) of the citrus fiber sample: x = 3c / [(100-m) / 100], for any given concentration c% w / w (samples start at 1.75% w / w, 5.00% w / w with 0.25% w / w increments). The moisture content m should be determined by infrared moisture balance (Sartorius MA 30), such as weight loss at 105 ° C with automatic timing, typically 3-4g of citric fiber covering the entire base of the aluminum pan. The moisture content (m) of citric fiber is in percentage by weight (% in p).
- Weigh in a second beaker of 600ml_ the required grams (w) of standard tap water, to the nearest 0.1 g, according to the humidity of the citrus fiber sample: w = 270.0-x
- Place the beaker with CPF in the laboratory balance, set the balance to zero, add 30.0 g (to the nearest 0.1 g) of ethylene glycol, because the beaker was balanced and mix the content with the plastic spoon of this humidifying the entire powder (this operation is performed within 60 seconds).
- Immediately pour the standard tap water into the wet citric fiber and mix the content with the plastic spoon by repeatedly clockwise and counterclockwise rotations (this operation is carried out within 60 seconds).
- Place the glass beaker with its content (citrus fiber, ethylene glycol, standard tap water) under an RWD 20 IKA Digital stirrer and lower the paddle (4 paddle propeller 07 410 00) in the paste until 2 cm from the base of the glass beaker———
- Adjust the paddle speed (rpm) to 900 rpm and stir 10 minutes at 19 rpm at 900 rpm.
- Cover the beaker with aluminum foil and allow to rest for 24 hours before measurement
- Pour the required amount of CPF dispersion into the cylindrical cup of the rheometer and immediately insert the ST24 vane probe (starch cell probe) into the cylinder containing the CPF dispersion Sample analysis
- Perform oscillatory CSS test with MCR301 according to manual instructions, with 2 segments:
segment 1: without logging, 10 minutes at 20 ° C (equilibrium) segment 2: logging, 1971 seconds at 20 ° C, 50 integration time of measuring points 100 to 10 seconds log, torque 1 to 10,000pNm log, frequency 1 Hz
Results
At low voltage where G * (counter voltage) is showing constant plateau values, calculating the average G * results in the linear viscoelastic range. Using the LVE Range software, the end of the linear viscoelastic region in the CSS experiments can be determined.
Outline the LVR G * against concentration. The first tangent in low concentration (below c *) has a much lower slope than the second tangent in high concentration (above c *). Using linear adjustment (for example with Microsoft® Excel®), the crossing point of both tangents occurs at the packaging concentration close to c *.
3. Measure viscosity
Add citric fiber to standardized water in a beaker with a paddle mixer to obtain a citrus fiber dispersion of 3% by weight with a total volume of 300 ml. Before adding the citric fiber, create a vortex by adjusting the blade speed to 900 rpm using an IKA RW20 Suspended Mechanical Stirrer equipped with a 4-blade propeller stirrer. Then add the citric fiber quickly (before viscosity constructions) to the walls of the vortex under agitation (900 rpm using an IKA RW20 Suspended Mechanical Stirrer equipped with a 4-blade heli16 / 19 ce agitator). Continue stirring for 5 minutes at 900 rpm. Store the sample for 12 hours at 20 ° C.
Then perform the viscosity test with a rheometer (for example Anton Paar MCR300), according to the instructions of the rheometer, depending on the shear rate (from 0.01 to 100 s' ¹ ) at 20 ° C.
Viscosity (mPa.s) is determined at a shear rate of 5 s' ¹
4. Emulsification
Prepare an emulsion containing 20% sunflower oil, 2% citric fiber fiber and the remaining standard tap water. First disperse the fiber in the water phase under a high shear mixture (8000 rpm) for 1 minute. Then add the oil to the water phase under high shear mixture (13500rpm) for 5 minutes at room temperature and constant speed.
Particle size distribution of the obtained emulsions is measured using dispersion of lamps (for example using a Malvern MasterSizer X). Typically, a bimodal particle size distribution is observed (see Figure 2a). The peak on the right corresponds to the particle size distribution of the oil-rich fraction of the emulsion (oil droplets + soluble fibers), while the peak on the left corresponds to the particle size distribution of the emulsion-rich fraction of the emulsion (by example cellulose).
The Malvern software allows the determination of an average diameter of total volume D (4.3), but it cannot provide the D (4.3) of the separate fractions. However, when the fractions show a normal log distribution, a peak deconvolution can be applied.
Peak deconvolution can be performed as follows: transfer the raw data from Malvern MasterSizer X in Microsoft Excel ™ for further analysis. It is assumed that the average diameter of the total volume (as obtained by Malvern MicroSizer) equals the sum of 2 normal log distributions.
The equation ... for a normal log distribution can be found in the literature. The normal log distribution is a distribution of two
17/19 parameters with parameters u 'and σ _τ . The probability density function for this distribution is determined by:
where = Τ ', Em (T), where the values of T correspond to the particle sizes in the present method, eu' = mean of the distribution σ _τ = standard deviation of the distribution
Deconvolution can be performed based on this equation and the results obtained are shown in Figure 2b.
A good fit is found between the distribution of raw data and the applied model. The mean (u ') of the peaks of each distribution corresponds to the D (4.3) of each phase (oil-rich and insoluble-rich). This assumption can be made due to the fact that the particles follow an almost normal dé log distribution; perfect.
5. Measure Color (CIELAB L *, b * values)
CIE L * a * b * (CIELAB) is the most complete color space specified by the International Commission on Illumination (Commission Internationale d’Eclairgé). It describes all the colors visible to the human eye and was created to serve as a device-independent model to be used as a reference. The values of L * and b * of the citric fiber are obtained by placing citric fiber (in the form of powder) in the glass cell (the cell is loaded around half) of the colorimeter and analyzes the sample according to the user's instructions. colorimeter. The colorimeter used is a Minolta CR400 calorimeter.
Examples
Several commercially available citrus fibers are compared before and after the process of the present invention:
1. Citri-Fi 100, orange fiber derived from orange pulp (Fiberstar
Inc.) _____________ ...
2. Herbacel AQ-plus Citrus Fiber F / 100, lemon fiber derived
18/19 of lemon peel (Herbstreith & Fox Inc).
3. Herbacel AQ-plus Citrus Fiber N, lemon fiber derived from lemon peel (Herbstreith & Fox Inc).
The fibers are adjusted with water to a dry matter content of 5% by weight and loaded into a pressure homogenizer (Niro Soavi, type NS3006L) and recirculated (maximum 0.5 MPa (maximum 5 bar)) while adjusting the pressure of supply at 70 MPa (700 bar).
The precipitation tank is loaded with a 1.8 m ³ centrifugal pump of 75-80% by weight of ethanol solution from the first wash tank. The homogenized fibers are sent directly to the precipitation tank with a volumetric pump. Shake while loading the tank, and continue to stir for about 30 minutes.
Adjust the speed of the centrifuge bottle (Flottweg centrifuge, 900R150, bottle Z23-3) at 5260 rpm. The differential speed is set at 30 rpm and the diameter setting at 145 mm. Load the product into the centrifuge bottle with a volumetric pump, and recover the product:
First ethanol wash: a tank is loaded with 1.5 m ³ of 82% by weight ethanol solution from the second ethanol wash. Then feed the recovered product into the tank, and stir for about 30 minutes. The washed product is then sent to a 100 pm rotary filter with a volumetric pump, and the product is recovered.
Second wash with ethanol: send the product recovered from the first wash with ethanol in a loaded tank of 1.4 m ³ of 85% by weight of ethanol solution, and stir for about 30 minutes. The washed product is then sent to a 100 pm rotary filter with a volumetric pump, and the product is recovered.
The product recovered from the second ethanol wash is then fed through a screw press. The speed and pressure are adjusted to obtain a dry matter content of about 30% by weight.
The product is then ground using a Lõdigue, 900M340, type FM300DIZ, and grind for 15 to 30 minutes.
The product is then fed into a vacuum dryer (E19 / 19
Cl) and mixed for about 90 minutes. Slowly add 40% (based on product matter) of a 60% ethanol solution. Dry with 95 ° C of water for 4 hours under vacuum.
Recover the orange pulp fiber.
1. packaging concentration close to c *
C * (before the process)% in p, anhydrous base C * (after the process)% in p, anhydrous base Citri-Fi 100 4.04 3.04 Herbacel AQ-Plus CitrusFiber N 3.94 6.74
2. Viscosity
Before processing(mPa.s) After processing(mPa.s) Citri-Fi 100 508 6345
In addition, an additional test was carried out. It was evaluated with mixing speed (versus 900 rpm used in the test method), about the same level of viscosity increase could be obtained for commercial citrus fiber. For the Citri-Fi 100 sample, a viscosity of 7545 mPa.s could be obtained if the citric fiber is dispersed in standardized water at high shear rates (9500 rpm). This shows the benefit of the process of the present invention in that it modifies the citrus fiber so that it can build up viscosity even when dispersed in solution at low shear rates. This means that the citrus fiber of the present invention is much easier to process and provides economic advantages (equipment and energy) over the prior art fibers.
3. Emulsification
D4.3 (pm) phaserich in oil D4.3 (pm) phaserich in insoluble Herbacel AQ-Plus Before processing 18.3 98.2 Citrus-Fiber F / 100 After processing 14.2 78.7
1/3

权利要求:
Claims (14)
[1]
1. Process to modify the characteristics of citrus fiber characterized by the fact of understanding the stages of
The. hydrate citrus fiber, having a dry matter content of
5 5% by weight or less,
B. mixing the hydrated citric fiber from step (a) with a process aid selected from the group consisting of enzymes, acids, bases, hydrocolloids, vegetable fiber, bleaching agents, and combinations thereof before homogenization;
C. homogenize the hydrated citric fiber from step (b) to obtain homogenized citric fiber, in which the energy input to perform homogenization is at least 1000 kW per cm ³ of citric fiber;
d. wash the homogenized citric fiber from step (c) with an organic solvent in a solid-to-solvent weight ratio of at least
15 minus 0.25: 1 to obtain citric fiber washed with organic solvent;
and. fragment or spray, and remove the solvent and dry the citric fiber washed with organic solvent from step (d); and
f. recover modified citrus fiber from it, said citrus fiber having a packaging concentration value C * less than
20 3.8% by weight, anhydrous base.
[2]
2. Process according to claim 1, characterized by the fact that said citrus fiber is obtained from citrus pulp, citrus peel, citrus pieces and combinations thereof.
[3]
3. Process according to claims 1 and 2, characterized by the fact that the viscosity of the modified citrus fiber is increased by at least 100%, in which said citrus fiber is dispersed in standardized water at a mixing speed of between 800 rpm to 1000 rpm, to a standardized 3% w / w citric fiber / water solution, in which the said viscosity is measured at a shear rate of 5 s ^_1 to 20Ό.
30
[4]
4. Process according to claims 1 to 3, characterized by the fact that the treatment comprises pressure homogenization using a pressure between 5 MPa to 100 MPa (50 bar to 1000 bar).
Petition 870180062802, of 07/20/2018, p. 8/15
2/3
[5]
5. Process according to claim 4, characterized by the fact that said treatment is a single step pressure homogenization using a pressure between 30 MPa to 100 MPa (300 bar to 1000 bar).
5
[6]
6. Process according to claim 4, characterized by the fact that said treatment is a homogenization of multi-pass pressure comprising at least 2 passages, using a pressure between 10 MPa to 60 MPa (100 bar to 600 bar).
[7]
Process according to any of claims 1 to 6,
10 characterized by the fact that the citric fiber is subjected to a heat treatment before homogenization at a temperature between 50Ό to 140Ό for a period of 1 second to 3 minutes.
[8]
8. Citric fiber, obtained by the process as defined in claims 1 to 7, wherein said citrus fiber has a moisture content
15 out of 5% to 15%.
[9]
9. Citric fiber according to claim 8, characterized in that it has a viscosity of at least 1000 mPa.s, wherein said citric fiber is dispersed in standardized water at a mixing speed of 800 rpm to 1000 rpm, preferably 900 rpm, to a solution of
20 citric fiber / standardized water at 3% w / w, and where said viscosity is measured at a shear rate of 5 s' ¹ to 20 a.
[10]
10. Citric fiber according to claim 8 or 9, characterized in that it has a CIELAB L * value of at least 90.
[11]
11. Citric fiber according to claim 10, characterized by the fact that it has a CIELAB b * value less than 20.
[12]
12. Mixture of citrus fiber characterized by the fact that it comprises a citrus fiber as defined in claims 8 to 11 and a fiber derived from plant.
[13]
13. Food product, food product, drink, personal care product, pharmaceutical product or detergent product characterized in that it comprises a citrus fiber as defined in claims 8 to 11 or a mixture as defined in claim
Petition 870180062802, of 07/20/2018, p. 9/15
3/3
[14]
14. Use of citrus fiber as defined in claims 8 to 11 or a mixture as defined in claim 12, characterized in that it is as a texturizer or viscosifier in food products, a food product, a drink, a care product folks,
5 a pharmaceutical product or a detergent product.
Petition 870180062802, of 07/20/2018, p. 10/15
1/2 improved citric fiber

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法律状态:
2018-03-20| B15K| Others concerning applications: alteration of classification|Free format text: AS CLASSIFICACOES ANTERIORES ERAM: A23L 1/212 , A23L 1/308 , A23L 1/30 Ipc: A23L 33/10 (2016.01), A23L 19/00 (2016.01), A23L 3 Ipc: A23L 33/10 (2016.01), A23L 19/00 (2016.01), A23L 3 |

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2018-04-03| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|

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2018-04-24| B07A| Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]|

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2018-09-04| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

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2018-10-16| 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 29/07/2011, OBSERVADAS AS CONDICOES LEGAIS. |

优先权:

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申请号 | 申请日 | 专利标题

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US36920710P| true| 2010-07-30|2010-07-30|

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EP10008316|2010-08-10|

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PCT/US2011/045993|WO2012016201A2|2010-07-30|2011-07-29|Process for modifying the properties of citrus fiber|

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