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EP2555639A1 - Obtention de particules par dispersion par centrifugation - Google Patents

Obtention de particules par dispersion par centrifugation

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Publication number
EP2555639A1
EP2555639A1 EP11715067A EP11715067A EP2555639A1 EP 2555639 A1 EP2555639 A1 EP 2555639A1 EP 11715067 A EP11715067 A EP 11715067A EP 11715067 A EP11715067 A EP 11715067A EP 2555639 A1 EP2555639 A1 EP 2555639A1
Authority
EP
European Patent Office
Prior art keywords
liquid
particles
density
layer
centrifugation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP11715067A
Other languages
German (de)
English (en)
Inventor
Albert Thijs Poortinga
Marcel Paques
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FrieslandCampina Nederland BV
Original Assignee
Friesland Brands BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Friesland Brands BV filed Critical Friesland Brands BV
Publication of EP2555639A1 publication Critical patent/EP2555639A1/fr
Withdrawn legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/02—Making microcapsules or microballoons
    • B01J13/04—Making microcapsules or microballoons by physical processes, e.g. drying, spraying
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/30—Encapsulation of particles, e.g. foodstuff additives
    • A23P10/35—Encapsulation of particles, e.g. foodstuff additives with oils, lipids, monoglycerides or diglycerides

Definitions

  • the invention relates to a method for preparing particles, to particles obtainable by a method according to the invention, to a food product comprising said particles, and to the use of said particles.
  • Particles have been defined and classified in various different ways depending on their specific structure, size, or composition.
  • particles are broadly defined as micro- or nanoscale particles which are typically composed of at least one solid, semi-solid or liquid material.
  • the weight-average diameter of such particles range from approximately 10 nm to approximately 1000 ⁇ , as may be determined by microscopy (light microscopy, or electron microscopy, depending on the size, as will be understood by the skilled person). More in particles, the term is used herein for particles having an average particle diameter between about 0.5 ⁇ and 100 ⁇ .
  • Particles may have a homogeneous structure or a heterogenous structure.
  • Homogenous particles in general consist of a material in a single phase (state of matter), e.g. one liquid phase or a material in a single solid state of matter Particles with a heterogeneous structure wherein two or more states of matter (phases) are distinguishable may be referred to as hierarchical particles.
  • Hierarchical particles in particular include particles comprising an inner core and an outer layer (a coating or shell or the like), such as nano- and microcapsules. They further include particles formed by the colloidal association of small molecules, especially of amphiphilic molecules, or other complex structures, such as liposomes, lipoplexes, lipid complexes, and lipospheres.
  • Particles are used in many fields. For instance, particles comprising an active substance, such as a medicine or a nutrient, are used in pharmaceutical respectively food applications.
  • an active substance such as a medicine or a nutrient
  • Particles with a hierarchical structure have various uses.
  • particles of an active substance such as a medicinal product or a nutrient
  • a protective layer as by means of encapsulation
  • a protective layer surrounding a pharmaceutically active ingredient or a food ingredient may also serve to alter a release pattern of said ingredient, after administration to an individual.
  • enteric coatings are known to provide sustained release preparations that delay release of an active substance until the orally administered preparation has passed the stomach.
  • the core may also comprise an active substance or be an inert phase (e.g. water).
  • an active substance e.g. water
  • Fat particles may also act as a structuring agent, e.g. in a cream or foam.
  • a similar effect as with full-fat particles may be achieved, whilst the fat content of the product is reduced.
  • a common technique for preparing particles is spray-drying is a conventional technique.
  • spray-drying typically, wet emulsions or dispersions are sprayed under pressure in a spray tower and then contacted with hot air.
  • spray- drying can cause problems as a result of a high thermal load of the product, which can lead to quality loss, in particular if the product contains a component which is heat- sensitive. Also, problems can occur with the controllability of the product properties such as particle size distribution, form and/or solubility; there is the risk of dust explosions. Further, the high energy consumption is a problem. In addition it is generally difficult to produce core-shell particles, especially small (10 micron or smaller) particles. Moreover particularly a need exist for particles with a hydrophobic (e.g. fat) shell in water. Producing these by spray-drying, e.g. in air, would imply that a subsequent dispersion step in water is needed which is impractical and may again destroy the particles.
  • a hydrophobic e.g. fat
  • Colloidosome particles can be prepared with the aid of an emulsion of the water-in-oil type or the oil-in-water type, see e.g. WO 02/47665.
  • a hydrophobic continuous phase such as toluene
  • the examples all use a synthetic polymer, such as polystyrene or polymethyl methacrylate. After allowing aggregation of the particles, if desired, the hydrophobic continuous phase may be replaced by water after the colloidosomes have been formed.
  • the colloidosomes need to be prevented from breaking as a result of the great forces exerted on the colloidosomes, for instance as a result of the surface tension.
  • the colloidosomes are washed first with octanol and then added to an aqueous solution of a surface -active substance.
  • the particles are usually strongly bonded to one another, for instance by sintering.
  • Known preparation techniques generally yield products wherein a substantial fraction of the particles do not have an essentially closed shell.
  • WO 97/16176 describes a method for forming microparticles (coated cell aggregates) by passing cell aggregates or air bubbles through layers of a density gradient.
  • the coating is a polymer layer, which is generally hydrophilic, and which is precipitated (solidified) by contacting the polymer with a non-solvent for the polymer.
  • the present inventors further observe that the cells to be coated should first be centrifuged through a polymer solution and should subsequently pass into a non- solvent layer needed to precipitate the polymers. This implies that the solvent and the non-solvent should be miscible to a sufficient extent. In the example of WO 97/16176, solvent and non-solvent are in fact even fully miscible.
  • JP 11 25355 A relates to a method similar to the method of WO 97/16176.
  • Particles in the form of core-shell double emulsion droplets can be produced using microfluidic methods (e.g. WO 2007/030501). Using these methods it is however difficult to produce small double emulsions droplets, e.g. smaller than 10 micron, since this requires microfluidic devices with very small features which will give rise to larger pressure drops, greater susceptibility to fouling, larger influence of the
  • the present invention relates to a method for preparing particles, comprising
  • the invention relates to particles obtainable by a method according to the invention. These particles are in general hierarchical particles.
  • the invention is in particular directed to a method for preparing core-shell particles.
  • the core-shell particles according to the invention are particles having at least one solid, liquid or gaseous core and an outer phase formed of the first liquid or solidified first liquid, at least substantially surrounding the core or cores.
  • a core-shell particle having a single core (2) and a single shell (1) is schematically shown in Figure 1.
  • the first liquid generally is present in the form of a layer on the surface of the core.
  • Figure 2 shows a particle with multiple cores (2) in a surrounding first liquid (1).
  • the first liquid generally not only forms a shell at least partially surrounding the assembly of cores but may also form layers between the individual cores and/or at least partially fill interstitial spaces between the cores.
  • the invention relates to a food product, comprising particles according to the invention.
  • the invention relates to the use of particles according to the invention as a fat substitute.
  • the invention in particular is suitable for preparing edible particles.
  • “edible” is particularly understood to mean “suitable for human consumption”, more in particular suitable for use in a food, including beverages, such as for instance in a dairy product, soup or a beverage.
  • a method according to the invention is suitable to provide particles comprising a liquid coating; particles comprising a non-polymeric coatings that can be solidified, e.g. by temperature reduction,, e.g. melts, in particular a lipid melts; particles having a core other than biological cells or gas bubbles, in particular particles comprising a liquid core; small particles ( ⁇ 50 ⁇ diameter), in particular capsules with a diameter of less than 50 ⁇ .
  • the core is liquid it is particularly advantageous to make the density of the core deviate from the density of the continuous phase that receives the microcapsules (e.g. the second phase in the above description).
  • the continuous phase may have a different hydropilicity than the coating material and/or the interfacial tension between coating material (which is preferably hydrophobic) and continuous phase (which is preferably hydrophilic) may be relatively high, preferably larger than 1 mN/m, in particular 2 mM/m or more, more in particular 3 mN/m or more.
  • the upper limit for the interfacial tension is not particularly critical. In principle it may be more than 20 mN/m. Usually it is 20 mN/m or less, in particular 10 mN/m or less.
  • the interfacial tension can be determined by drop tensiometery.
  • a liquid or gaseous state of a substance m this state under the existing method conditions is meant, unless specified otherwise.
  • the compound will be a solid below the melting point and liquid between the melting point and the boiling point, and a gas above the boiling point (at a given pressure).
  • Mixtures of compounds do not always have a specific melting point, but may rather have melting ranges (e.g. fats).
  • melting ranges e.g. fats
  • 'solid' is used herein in particular in relation to a method according to the invention means to indicated that a substance under the existing method conditions is essentially shape and volume stable, e.g. a material in a solid state of matter or an edible solid material such as a spice, herb, mineral, peptides, amino acids, cells, etc.. If the term 'solid' is used in another context ⁇ e.g. that particles are solid at room temperature), this will be specified.
  • liquid' is used herein in particular in relation to a method according to the invention means to indicated that a substance under the existing method conditions is able to flow and take the shape of a container, but, like a solid, it resists compression and does not disperse to fill every space of a container, and maintains a fairly constant density.
  • liquids include in particular liquids in the sense of one of the three classical states of matter.
  • a liquid may be formed of a single compound or a mixture of several compounds. If the term 'liquid' is used in another context ⁇ e.g. that a lipid is liquid at room temperature), this will be specified.
  • fat is generally used herein as a generic term for carboxylate esters of glycerine (glycerides); in particular triglycerides are fats.
  • glycerides glycerides
  • triglycerides are fats.
  • fat includes compounds that are solid at room temperature and compounds that are liquid at room temperature (20 °C).
  • oil is used to describe that the fat is liquid.
  • the oil in the oil in water emulsion comprises one or more fats which form a liquid phase at the processing temperature during at least part of the method.
  • 'at least substantially is in particular meant 'for 50-100 %', more in particular 'for 80-100 %', more in particular 'for 85-100 %', for '90-100 %' or 'for 95- 100 %'.
  • water when referred to herein to 'water', in particular as part of a phrase like oil-in-water(-in-oil), or water-in-oil(-in-water), the term water is used broadly and includes aqueous liquids.
  • a method of the invention may be employed at a relatively low temperature, e.g. around room temperature, which is advantageous with respect to energy consumption and/or in case the particles are prepared from a heat-sensitive material, or at an elevated temperature, e.g. between room temperature and the boiling point of the liquids.
  • a method of the invention is suitable to collect hierarchical particles, optionally dispersed in a collection phase in a relatively pure form, if desired.
  • relatively pure form is meant that the collected particles are at least substantially free of droplets consisting of the first liquid (or solidified first liquid) and material that has not been provided with a layer formed of the first liquid (or solidified first liquid).
  • a method of the invention can be employed adequately at a high production capacity, and is advantageous in that respect compared to at least some known methods, such as the use of microfluidic devices.
  • a method according to the invention allows preparation of hierarchical particles with a high encapsulation efficiency, at least compared to some other encapsulation techniques, e.g. a known technique wherein the particle formation is (primarily) done by emulsification dispersing.
  • a method according to the invention is advantageous in that it allows the preparation of core-shell particles with (essentially) complete enclosure of the core or cores by a shell.
  • a method according to the invention advantageously allows fine- tuning in a controlled manner of thickness of the shell, in case core-shell particles are prepared.
  • said dispersion comprising dispersed material and the first liquid may be dispersed into the second liquid prior to the centrifugation. This is generally done by gentle mixing under conditions wherein no substantial microparticle formation occurs, e.g. by shaking manually.
  • the dispersed first fluid and the dispersed material dispersed therein will be pulled in an opposite direction by the centrifugal force.
  • the dispersed material will be dragged out of the droplets of the first fluid towards the second fluid therewith taking along a thin layer of first fluid surrounding the dispersed particles. This is illustrated schematically in Figure 9B.
  • embodiment is advantageous at least in specific embodiments as this increases the amount of interfacial area in-between the coating liquid and the continuous phase making it easier to transfer the core through the interface. Also it assures that the cores have to travel for only a short distance before they reach the interface and a microcapsule is formed. This makes coating proceed faster. In particular in a continuous method according to the invention this is considered to be favourable in order to reduce the chance of particles to deteriorate in the centrifuge.
  • said dispersion and the second liquid are applied into the centrifugation chamber as separate layers prior to or during centrifugation (the latter in particular in case of continuous centrifugation).
  • the first layer comprising the dispersion and a second layer comprising the second liquid are then in general applied such that during centrifugation the first layer is situated closer to the centre of rotation than the second layer.
  • the first layer comprising the dispersion and a second layer comprising the second liquid are then in general applied such that during centrifugation the first layer is situated more remote from the centre of rotation than the second layer. This is illustrated schematically in Figure 9A.
  • the hierarchical particles are formed during centrifugation.
  • the centrifugation chamber typically rotates around a centre of rotation (the rotational axis).
  • the dispersion (comprising the first liquid) and the second liquid rotate in separate layers around the centre of rotation.
  • the particle preparation in accordance with the invention is based on the insight that it is possible to employ a centrifugal force to move the dispersed material out of the phase wherein it has been dispersed (at least comprising the first liquid) into the second liquid. When the material actually migrates into the second liquid, it will at least substantially be surrounded by a film comprising the first liquid.
  • a second liquid with a specific density is selected.
  • a second liquid is generally provided that has a density that is higher than the density of the first liquid yet lower than the density of said material.
  • the dispersion of the dispersed material in the first liquid will then be positioned (in a first layer) closer to the centre of rotation than the second liquid (in a third layer).
  • the material be able to leave the first liquid and also to penetrate into the second liquid, whereby particles are formed of said material, at least substantially surrounded by a film comprising the first liquid.
  • Such embodiment is in particular useful for various liquid materials or (dense) solid materials.
  • a second liquid is generally provided that has a density that is lower than the density of the continuous phase yet higher than the density of said material.
  • the dispersion of the dispersed material and the first liquid will then be positioned more remote from the centre of rotation than the second liquid.
  • the material be able to leave the first liquid and also to penetrate into the second liquid, whereby particles are formed of said material, at least substantially surrounded by a film comprising the first liquid.
  • the dispersed material may for example be a gas or low-density solid particles (such hollow particles comprising internal voids filled with gas).
  • densities and viscosities may be chosen in such a way that:
  • the dispersed material will, under the influence of the centrifugal force, move from the first fluid phase to the interface with the second fluid within an acceptable time.
  • ⁇ is the viscosity of the first fluid phase in mPas, which will usually be about 10 2 mPas (being the order of magnitude of the viscosity of oil)
  • the core will travel through the first fluid towards the interface at a speed v in the order of 1 mm/s. This means that for a practical height of the first liquid phase of a few centimeters the cores need up to 1 min to travel to the interface between the first in the second fluid where they will form a core-shell. This is a very practical time, such that condition 1 is fulfilled.
  • the density of the dispersed material in the dispersion is usually at least 1.05 times, in particular at least 1.10 times the density of the continuous phase, if the dispersed material is more dense, respectively up to 0.95 times, in particular up to 0.90 times the density of the continuous phase if the dispersed material is less dense.
  • the differences in density between the first liquid and the second liquid are not particularly critical.
  • the difference in density may be 2 % or more.
  • the differences in density between the dispersed material (or of the formed particles, if those have a substantially different density) and the second liquid are not particularly critical.
  • the difference in density may be 2 % or more.
  • the maximum difference is not critical, the higher the difference, the lower the centrifugal force needed to prepare the particles at a specific rate.
  • the density of the more dense of the dispersed material and the continuous phase, respectively the first and the second liquid respectively the dispersed material and the second liquid is not particularly critical, it may for instance be up to 5 times, up to 3 times, up to 1.5 times, or up to 1.25 times the density of the less dense of these two phases.
  • the density difference of the second liquid and the dispersed material (or of the formed particles, if those have a substantially different density) it is observed that in particular if the second liquid serves as a collection phase a relatively small difference can be advantageous for collecting purposes. Also a relatively small difference may be advantageous with respect to avoiding disruption of the formed particles, while centrifugation is continued.
  • a minimum centrifugal force to cause the dispersed material to move out of the continuous phase can be determined based on the information disclosed herein, common general knowledge and optionally a limited amount of testing. In general, centrifugation will be carried out at 50 g or more, in particular at 250 g or more, more in particular at 1000 g or more. A suitable maximum limit is determined by the centrifugal force at which the prepared particles are disrupted to an unacceptable extent. Depending on the specific dispersed material and liquids used the maximal centrifugal force may be 100 000 or more, 500 000 or more, or even 1 000 000 or more, whilst still obtaining particles in accordance with the invention. However, good results can be obtained with a method wherein the centrifugal force is less than 50 000 g, less than 25 000 g , or less than 10 000 g.
  • the centrifugal force that is actually employed is usually mainly determined by the average particle size of the desired particles. In general a certain minimum centrifugal force is needed to achieve formation of the shell around the core with a good degree of coverage. The minimum centrifugal force that is needed is higher as the size of the dispersed particles or droplets decreases.
  • Figure 3 a relation between centrifugal force and particles size of core-shell particles is illustrated for particles wherein the core is liquid.
  • the line 'g min' shows which centrifugal force according to the above exemplary model is needed to produce core- shell particles with the diameter shown at the x-axis.
  • a different method conditions nature of the used material and liquids, etc.
  • centrifugal force may be applied in order to obtain a desired average particle size.
  • the size of the obtained core-shell particles is primarily determined by the size of the material ⁇ e.g. solid particles or liquid droplets) dispersed in the first liquid provided that the applied centrifugal force is large enough to transfer these through the interface between the first and second liquid. This is in fact one of the prowess of the present invention.
  • the invention thus provides an
  • the encapsulation method for preparing core-shell particles that adjusts itself to whatever is provided as the material for the core (the dispersed material). For instance, if a material for the cores is provided with a specific particle size distribution, this usually essentially determines the particle size distribution of the formed core-shell particles, which may be essentially maintained. This can be very handy, e.g. for encapsulation of specific medicaments, minerals, biological cells.
  • a relatively high centrifugal force may also be preferred for an increased particle production rate.
  • the pressure that the core and the shell exert on each other in the centrifugal field may become so high that it overcomes the stabilising pressure (also known as disjoining pressure) of the used emulsifiers and the shell may rupture (Significant deformation of the core-shell particles may occur, or droplets of first liquid that are free of said dispersed material may form, e.g. due to disruption of prepared particles. This may be undesired.
  • a maximum value of a centrifugal force in a specific embodiment may be determined by the maximally allowable concentration of droplets of first liquid that are free of said dispersed material, in the collected particles.).
  • the centrifugal force is usually chosen to be less than the force of the disjoining pressure, which may be determined by routine testing.
  • the line 'g max' in Figure 3 shows such threshold centrifugal force for an exemplary model embodiment, wherein the core for the particles (which may be droplets) have been stabilised using an emulsifier.
  • the 'g-max' line will be different.
  • particulate stabilisers e.g. fat nanoparticles
  • the 'g max' line will be at least 10-100 times higher..
  • a preferred centrifugal force depends on factors like particle size of the dispersed material (for liquid dispersed material), desired thickness of the film formed of first liquid at least partially surrounding the material migrating out of the continuous phase, the nature of the dispersed material and the first liquid, e.g. density, physical/chemical interaction between said material and the first liquid, physical state of the dispersed material (liquid/solid/gas), viscosity of the first liquid and the dispersed material (if liquid), the presence of additives that stabilise the formed particles.
  • the centrifugation may be carried out in a continuous manner or in a batch manner.
  • the dispersion comprising the first liquid and the dispersed material
  • the second liquid and if used the collection phase may be applied to the centrifugation chamber in separate layers prior to centrifugation, wherein the phase with the highest density (the second liquid or the collection phase) is applied as the bottom layer and the phase with the lowest density as the top layer (the dispersion).
  • the phases with the highest density the second liquid or the collection phase
  • the phase with the lowest density as the top layer
  • a method according to the invention is also particularly suitable to be carried out in a continuous manner.
  • the dispersion, the second liquid, and - if used - a separate collection phase are applied to the centrifuge continuously or intermittently while continuing the centrifugation and particles are collected continuously or intermittently while centrifugation is continued.
  • Continuous centrifugation is particularly useful for preparing particles at a large scale, (see e.g. Perry's handbook of chemical engineering (1984), fig. 19-120a or Perry's handbook of chemical engineering (20 th edition), fig. 18-154a or fig 18-155.
  • centrifugation is continued as long as is needed to obtain the particles in a desirable yield.
  • a suitable centrifugation time (or average residence time in the case of continuous centrifugation) can be routinely determined with the help of the information disclosed herein and common general knowledge, and may . in particular be at least 10 sec, at least 25 sec at least 1 min, up to 10 min or more, up to 30 min or more or up to 1 hr or more.
  • the centrifugation time is chosen just long enough to achieve the particles formation at a desirable yield, to minimise the risk of a substantial portion of the formed particles being disrupted by the centrifugal field.
  • a suitable time can be determined depending upon the specific situation, based on the information disclosed herein and common general knowledge.
  • the particles may be collected as a dispersion of the second liquid or isolated from the second liquid.
  • a collecting-phase for the particles in the centrifugation chamber is also possible to provide a collecting-phase for the particles in the centrifugation chamber.
  • this phase is chosen to have a density that will allow the particles to migrate from the second liquid into the collection phase.
  • the collection phase has a density that is higher than the density of the second liquid if the particles have a higher density than the second liquid respectively a density lower than the second liquid if the particles have a lower density than the second liquid.
  • a density of the collection phase that is about the same as the density of the prepared particles is in particular advantageous to collect particles because this will (essentially) stop the core-shell particles from continuing to move into the centrifugal field.
  • the concentration of the particles when collected in the second liquid or the collection phase is not critical; they may be collected in a relatively low concentration in the second liquid or the collection phase, e.g. in a concentration of 1-10 % a, based on the total weight of the collected product , if desired the particles may be collected at a higher concentration, e.g. of more than 10 %, in particular up to 50 %, based on total weight.
  • a relatively low concentration is considered advantageous with respect to maintaining particle shape and integrity, in particular in case the particles have a liquid core and/or liquid outer layer. It may also be advantageous to collect at a relatively low concentration in order to avoid or at least reduce coalescence of the outer phase (which may still be liquid).
  • At least part of the layer comprising the first liquid of the prepared particles is solidified before, during or after collecting the particles.
  • Solidification may usually be accomplished by extracting a solvent from the first liquid ⁇ e.g. when the first liquid is a polymer solution) or by cooling the particles to a temperature below the solidification temperature (or range) of the first liquid. This may be done after centrifugation or during centrifugation, e.g. by maintaining the dispersion layer at a temperature above the solidification temperature (or
  • solidification range of the first liquid and maintaining the second liquid, or (if present) the collection phase at a temperature below the solidification temperature (or solidification range).
  • the collected particles may be further treated, e.g. subjected to a concentration step.
  • concentration may for instance be carried out by filtration ⁇ e.g. tangential flow filtration) or a further (gentle) centrifugation step.
  • a suitable centrifugal force is usually lower than the centrifugal force needed during formation of the core-shells (see Fig. 3), preferably at least 10 times lower, in order to (nearly) completely rule out substantial destruction of the core-shells.
  • the minimum required force depends on the particle size, particle density, density of the fluid in which the particles are dispersed and viscosity of said fluid, and can be determined routinely.
  • the collected particles may be used whilst dispersed in the second liquid, the collection phase, or yet another phase, or may be isolated there from, prior to further use.
  • a liquid lipid can be used, more in particular an edible fat that is liquid under the centrifugation conditions.
  • Edible fats in particular include triglycerides. These are usually provided as a mixture of different triglycerides.
  • the fat may be of vegetable or animal nature.
  • the first liquid may comprise one or more fats selected from the group of milk fat, corn oil, cottonseed oil, canola oil, olive oil, peanut oil, safflower oil, soybean oil, sunflower oil, oils from nuts, oils from fruit seeds, and fractions of any of these fats and oils.
  • the melting range of the first liquid can be altered by changing the triglyceride
  • the centrifugation is in general carried out at a temperature above the melting range of the first liquid, but after the particles have been formed, the first liquid surrounding the inner material may be allowed to solidify, by reducing the temperature to a value at which the liquid or part thereof solidifies, if desired. This may be done during centrifugation, by maintaining the first liquid at a higher temperature than the second liquid (or at a higher temperature then a further phase, wherein the particles may be collected, see below).
  • the first fluid may also consist of a polymer solution or a polymer melt .
  • a polar liquid may be used that does not or at least not substantially form a single dissolved phase with the first liquid.
  • aqueous liquid is a liquid that comprises water as a major constituent. Usually at least 50 wt. %, in particular at least 80 %, more in particular at least 90 wt. % of the aqueous liquid is water.
  • the aqueous liquid may comprise one or more other polar liquids, e.g. ethanol, glycerol. Such liquids may e.g. be used to alter the viscosity and/or the density of the second liquid and its interfacial tension with the first liquid.
  • the first liquid is a polymer solution
  • a solvent that is at least partially miscible with a collection phase one could use a second fluid that is not miscible with this solvent, or one could already saturate the second fluid with this solvent.
  • the solvent will be extracted from the polymer solution shell such that it solidifies.
  • a separate collection phase for the particles which may be used in addition to the second liquid, may have largely the same composition as the second liquid, with the proviso that it is modified to keep the collection phase phase- separated from the second liquid.
  • the density and/or viscosity may be altered.
  • the collection phase may be a gel composed of the second liquid (or another liquid) and a gelling agent.
  • the first, the second or— if present - the third liquid may comprise one or more additives.
  • additives may in particular be selected from viscosity modifiers, density modifiers, gelling agents, dispersants (in particular emulsifiers), stabilising agents that stabilise the layer provided by the first liquid. It is also possible to influence the production of particles with either single or multiple cores e.g. by choosing the surfactant in the second phase in combination with the number of g's applied. If the combination of interfacial tension and g force is such that single core can not be drawn through the interface, multiple cores will collect the interface until the cumulative g-force becomes large enough to pull them through the interface therewith forming a multiple core particles. This can be seen in Example 3.
  • Viscosity modifiers and gelling agents are generally known in the art and include various polymers, e.g. polysaccharides (such as starch, cellulose, pectin, maltodextrins, derivatives of any of these), proteins.
  • polysaccharides such as starch, cellulose, pectin, maltodextrins, derivatives of any of these
  • Density modifiers are generally known in the art and include other solvents like glycerol, ethanol, solutes like carbohydrates, proteins, salts or nano- / micr oparticle s .
  • solutes are dissolved.
  • solutes with a relatively high molecular weight (> 500 g/mol) the osmotic pressure of the dispersed droplet will remain low which prevents swelling of the core-shells.
  • very small particles may be dispersed in the core phase to increase its density.
  • Dispersants are generally known in the art and include surface active agents, in particular emulsifiers, such as monoglycerides, diglycerides, phospholipids polymeric emulsifiers such as modified celluloses, modified starches, other modified carbohydrates, polysorbates (e.g. Tweens), fatty acids, esters of monoglycerides with sorbitan, lactic acid (lactem), acetic acid (acetem), citric acid (citrem), etc. , esters of fatty acids with sorbitan (Spans), polyglycerol esters of polycondensed fatty acids, in particularpolyglycerol polyriconoleate (PGPR), sodium stearoyl lactylate (SSL), proteins.
  • surface active agents in particular emulsifiers, such as monoglycerides, diglycerides, phospholipids polymeric emulsifiers such as modified celluloses, modified starches, other modified carbohydrates, polysorbates (e.g. Tweens
  • Modified carbohydrates may in particular be carbohydrates derivatised with a hydrophobic functionality and optionally an ionic functionality.
  • Particularly, predominantly fat-soluble emulsifiers are used in the hydrophobic phase and water- soluble emulsifiers are used in the hydrophilic phase.
  • the emulsifiers are used in a suitable concentration to have a interfacial tension lowering effect at the interface between the coating liquid and the continuous phase.
  • the emulsifier is used at a concentration at which the interfacial tension lowering effect is about maximal (typically ⁇ 10 % from maximum). This typically implies
  • Dispersants may be used to stabilise the particles. It is contemplated that in particular spacer particles or particles that stabilise the interface between the layer formed by the first liquid and the material the layer at least partially surrounds and/or the interface between the layer of the first liquid and the environment are advantageous. Such particles may be selected from fat particles (crystals,
  • Suitable stabilising fat particles generally have a melting
  • the particle size of such particles will be less than the desired size of the layer formed by the first liquid.
  • Such particles are e.g. known from N. Garti et al., JAOCS 76 (1999) 383-389).
  • Stabilising fat particles are in particular considered advantageous to stabilise the interface of the material forming the core(s) of the particles and the layer of the first liquid in case said material is water or an aqueous liquid and the first liquid is an oil.
  • Spacer particles may also be used to modify the thickness of the shell of a core-shell particle.
  • an emulsifier may be used to create a lamellar phase and therewith form multiple layers around the dispersed material, in case the dispersed material are droplets of water or an aqueous liquid, see e.g. Modern aspects of emulsion science (1998, B.P. Binks (ed)) p 236 for details on this principle.
  • an emulsifier that forms inverse micelles in the continuous phase in order to induce 'stratification' may be used, see e.g. Modern aspects of emulsion science (1998, B.P. Binks (ed)) p 336 or p345) for details on this principle.
  • the dispersed material may in principle be any substance of combination of substances.
  • the material may be selected from the group of gases (such as CO2, nitrogen, oxygen, air, a gaseous aroma) , liquids (water, aqueous liquids, emulsions), solids, mixtures of a solid and a liquid, mixtures of a solid and a gas, mixtures of a liquid and a gas and mixtures of a solid, a liquid and a gas.
  • gases such as CO2, nitrogen, oxygen, air, a gaseous aroma
  • liquids water, aqueous liquids, emulsions
  • solids mixtures of a solid and a liquid, mixtures of a solid and a gas, mixtures of a liquid and a gas and mixtures of a solid, a liquid and a gas.
  • the dispersed material comprises a compound selected from the group of proteins, other peptides, carbohydrates, vitamins, minerals (e.g. iron containing minerals), probiotics, prebiotics, salts, flavourings; aromatic substances, (phospho-)lipids, herbs, pharmaceuticals and spices.
  • a surrounding layer of the first liquid which may have been solidified, e.g. against detrimental influences of the environment during storage. Further, the presence of a surrounding may be desirable to achieve a desirable release pattern, before, during or after consumption.
  • the concentration of dispersed material as a weight percentage of the dispersion can chosen within wide limits. Usually the concentration is 0.1 wt. % or more, in particular 0.5 wt. % or more, more in particular 1.0 wt. % or more. The concentration may e.g. be 50 wt. % or less, in particular 24 wt. % or less.
  • a relatively low concentration of dispersed material is considered advantageous for allowing the centrifugal force to cause migration of the dispersed material (the cores for the core-shell particles that are formed) into the second liquid at an advantageous rate, especially if use is made of a method wherein the dispersion of the first liquid and material for the cores of the core-shell particles to be formed is dispersed in the second liquid prior to centrifugation. Therefore, it is specifically preferred that the concentration of dispersed material in the continuous phase comprising the first liquid is 20 wt. % or less, in particular 10 wt. % or less, or 5 wt. % or less.
  • the material (core) that is at least partially surrounded by the first liquid (that may have been solidified) serves as an (inert) carrier for the surrounding layer, which may in particular be a fat layer (provided by an oil used as the first liquid).
  • a fat layer provided by an oil used as the first liquid.
  • E.g. water, aqueous liquids, but also peptides, carbohydrates, dietary fibres, minerals, vitamins and other materials other than lipids may be used to that purpose.
  • particles are provided that can be used to partially substitute fat in a food product.
  • a method according to the present invention is highly suitable to provide hierarchical particles wherein the outer phase (the phase comprising the first liquid or solidified first liquid) forms a relatively small volume fraction of the total particle.
  • the particles may comprise 80-99.5 vol. % of said material and 0.5-20 vol. % may be formed of said first liquid which first liquid may have been solidified, based on total weight, more in particular 85-99 vol. % of said material and 1-15 vol. % of said first (solidified) liquid, based on total weight, even more in particular 90-98 vol. % of said material and 2- 10 wt. % of said (solidified) first liquid, based on total weight.
  • Corresponding weight percentages can be determined based on the respective densities.
  • a low volume fraction for the outer layer is in particular advantageous if the surface of the particles is of primary importance for the function of the particles, and wherein the outer phase is expensive, scarce, or wherein it is desired that the particles comprise little of the outer phase for health reasons (e.g. if the particles are used as a fat substitute).
  • the particle size of the particles according to the invention can be chosen within a wide range.
  • the particles have a volume-to-surface mean particle diameter d32 of at least 0.5 ⁇ , in particular of at least 2 ⁇ , at least 3 ⁇ or at least 5-10 ⁇ .
  • the particles have a volume-to-surface mean particle diameter d32 in the range of less than 500 ⁇ , preferably of 100 ⁇ or less, in particular of 50 ⁇ or less, more in particular 20 ⁇ or less, or 10 ⁇ or less.
  • the particles size can be determined using (dynamic) light scattering.
  • the particles of the invention are oil-in-water or oil in aqueous liquid emulsion droplets, which droplets are surrounded by an oil layer.
  • these droplets are present in an aqueous phase, i.e. water-in-oil-in water droplets are made.
  • the oil phase can in particular be selected from the oils mentioned above for the first liquid.
  • the particles comprise a shell that comprises a fat phase that is solid at 25 °C (such as fat crystals, e.g. milk fat crystals) and a fat phase that is liquid at 25 °C.
  • the particles comprise a shell that comprises spacer particles.
  • particles comprise one or more cores comprising a mineral, such as an iron containing mineral, like iron pyrophosphate.
  • the core-shell structure contributes to a controlled release pattern of the particles in food or pharmaceutical application, in particular after ingestion into the gastro-intestinal tract.
  • Particles according to the invention may in particular be used for the preparation of food products.
  • particles with a non-fat core and a fat- outer surface may provide the food product with fat-like organoleptic properties, whilst less fat is needed than when full-fat particles are used.
  • the invention is further directed to food product comprising edible particles according to the invention.
  • Such food product may in particular be selected from the group of foods comprising a gelled-structure, with dispersed therein the particles; whippable/whipped creams; cheeses; yoghurts; mousses; puddings;
  • bakery creams desserts; dairy beverages; ice creams; creamers (for coffee, soup or the like); toppings; cream bases; and meringues.
  • the invention is directed to a method for preparing a food product, wherein edible particles obtained in or obtainable by a method according to the invention are combined with one or more further food ingredients in a process for preparing the food in a manner that is otherwise known per se, e.g. it may be combined with one or more other food ingredients which combination can then be further processed to product the food product of interest.
  • particles according to the invention may be used in the preparation of a whippable cream by combining the particles with other cream ingredients (e.g. sugar, dairy protein, fat globules). Upon whipping the cream, the particles become part of the network structure of the whipped cream, thereby stabilising the whipped product.
  • cream is widely used in food industries. Cream is a three phase system, which, depending on numerous system parameters, can be transformed into a four phase system upon introducing air by whipping. Natural cream has in general good whipping characteristics in terms of whipping time, stability, overrun and firmness.
  • the emulsion droplet surface is covered by a milk fat globule membrane (MFGM) and the fat phase contains milk fat. Both the MFGM and the milk fat plays a crucial role in creating a whipped cream.
  • MFGM milk fat globule membrane
  • partial coalescence of the emulsion droplets should occur upon whipping.
  • spreading of liquid fat on the oil/air interface and creation of a solid fat network stabilizes the air bubbles.
  • the occurrence of partial coalescence is influenced by the stability of the interfacial layer (e.g. a MFGM or proteins) by the ratio liquid solid fat and most likely by the fat morphology (shape, size, stability, degree of sintering).
  • the particles according to the present invention are thought to provide a unique structural alternative for partial coalescence.
  • the particles collide with each other (and included air bubbles), followed by coalescence of the shell phases of both particles involved.
  • the presence of the cores restricts the coalescence to the thickness of the shell layers due to spatial interference, limiting the coalescence to partial coalescence.
  • This mechanism provides a structural alternative for the partial coalescence occurring as known for natural dairy cream. In order to allow this mechanism to proceed well it is important that the ratio between the core and the shell dimensions can be accurately tuned, particularly in the region where the shell thickness is thin in comparison to the diameter of the core.
  • the present invention allows such fine-tuning.
  • the particles may also advantageously be used in a gelled food product, e.g. cheese or a cheese analogue, wherein the particles are dispersed in a gel-matrix (e.g. gelled protein or carbohydrate) and act as structure disruptors.
  • a gel-matrix e.g. gelled protein or carbohydrate
  • the particles may be used to tune the mechanical bulk properties.
  • the particles are in particular suitable to impart a food product with a sensory quality that resembles a food product wherein fat is fully or predominantly present in the form of full-fat globules, having a higher fat content than the food product of the invention.
  • the particles are in particular suitable to impart a fat-associated sensory quality to the product, whilst requiring less fat than when use would be made of full fat particles.
  • Said sensory qualities may for instance be selected from
  • fatty oral texture an indication of how fatty the oral texture is perceived
  • one or more other sensory quality may be altered, in particular one ore more attributes selected from elasticity, hardness, dryness, graininess, smoothness, remainings, fracturability and fatty impression.
  • EP-A 1 884 166 EP-A 1 884 166.
  • the particles of the invention may be used for preparing a soft-solid food product— in particular a
  • soft-solid dairy food product such as a cheese product or a cheese analogue product— comprising
  • a mixture comprising particles according to the invention ⁇ e.g. a dispersion thereof in water or an aqueous liquid) and a gel, said gel comprising a protein;
  • the product comprises a gel phase comprising the protein, said gel phase having a relatively low fat content, and inhomogeneously distributed outside the gel phase a plurality of particles according to the invention.
  • suitable conditions may be based on EP-A 1 884 166.
  • a 50 wt% solution of maltodextrin 33DE (Roquette) was emulsified at a concentration of 1 wt.% in sunflower oil containing 5-10% Admul WOL (PGPR) as an emulsifier. Emulsification was such that water droplets of about 20 micron were formed. This emulsion was placed on top of a two layer system with the bottom layer containing 1 wt.% Tween 20, 30 wt.% maltodextrin and 1.5 wt% HM Pectin (CP kelco) and the top layer containing just 1 wt.% Tween 20.
  • PGPR Admul WOL
  • centrifuge tubes with a diameter of 3 cm were used.
  • Each of the three fluid phases (the w/o emulsion at the top, the emulsifier solution in the middle, and the maltodextrin+pectin+emulsifier solution at the bottom) had a height of about 1 cm. Centrifugation was done for 30 seconds at 1000 to 3000g.
  • Example 3 was carried out as Example 1, but with the middle phase replaced by a 1% sodium caseinate solution. Here capsules with multiple water cores were formed, as shown in Figure 7.
  • Example 4
  • Example 3 was carried out as Example 1, but replacing the sunflower oil with a molten fractionated palm oil (melting point of 53°C), using a warm (60°C) middle layer and a cold (5°C) bottom layer. Results are shown in Figure 8. Herein the liquid palm oil surrounding the aqueous core is solidified in the bottom layer, also serving as the collecting phase.
  • Example 5
  • Particles are continuously prepared in a continuous centrifuge, e.g a continuous disk- centrifuge bowl as shown in Perry's handbook of chemical engineering (1984), fig. 19- 120a.
  • the dispersion (w/o emulsion) comprising the material for forming the core (droplets of aqueous liquid) of the particles and the first liquid (an oil forming the continuous phase) is fed continuously into the centrifuge, thereby maintaining a first layer (a dispersion of the core in the continuous phase), said layer situated more remote to the centre of centrifugation.
  • the second liquid (an aqueous phase) is continuously fed into the centrifuge, thereby maintaining a second layer, said layer situated more close to the centre of centrifugation.
  • aqueous droplets migrate from the first layer into the second layer they drag along a film of the first liquid into the second liquid, whereby particles of aqueous liquid surrounded by an oil film are obtained in the second liquid. Together with the second liquid these particles form a double emulsion (of the w/o/w type).
  • two streams are collected: 1) the heavier stream containing formed double emulsions, 2) a rest stream partially or fully depleted from water, and rich in oil.

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biophysics (AREA)
  • Molecular Biology (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing Of Micro-Capsules (AREA)

Abstract

Cette invention concerne un procédé d'obtention de particules consistant : (a) à utiliser une dispersion comprenant une phase continue composée d'au moins un premier liquide, et, à l'état de dispersion dans cette phase continue, un matériau dispersé, la phase continue ayant une densité différente de celle du matériau dispersé ; (b) à utiliser un second liquide qui est au moins sensiblement immiscible avec le premier liquide et dont la densité est différente de celle du premier liquide ; (c) à placer la dispersion et le second liquide dans une chambre de centrifugation ; et (d) soumettre la chambre de centrifugation remplie de la dispersion et du second liquide à une centrifugation, ledit matériau entouré au moins partiellement d'une phase qui comprend un premier liquide émigrant de ce premier liquide vers le second liquide pour former des particules et ladite phase comprenant le premier liquide qui entoure au moins partiellement ledit matériau, dans le second liquide ; et (e) à recueillir les particules.
EP11715067A 2010-04-09 2011-04-08 Obtention de particules par dispersion par centrifugation Withdrawn EP2555639A1 (fr)

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NL2004533A NL2004533C2 (en) 2010-04-09 2010-04-09 Particle preparation by centrifugal dispersing.
PCT/NL2011/050232 WO2011126368A1 (fr) 2010-04-09 2011-04-08 Obtention de particules par dispersion par centrifugation

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US20130251855A1 (en) * 2012-03-21 2013-09-26 Pepsico, Inc. Aqueous product comprising oil-containing microcapsules and method for the manufacture thereof
GB2520370B (en) 2014-05-01 2016-09-14 Frito Lay Trading Co Gmbh Snack food seasoning
GB2520371B (en) * 2014-05-01 2016-09-14 Frito Lay Trading Co Gmbh Snack food seasoning
KR20190137882A (ko) * 2017-05-01 2019-12-11 카운슬 오브 사이언티픽 앤드 인더스트리얼 리서치 원심 분리기를 사용하는 금속 나노입자 또는 나노와이어의 계면 분리 공정
CN118718911A (zh) * 2024-07-04 2024-10-01 山东大学 一种基于密度梯度液柱快速固化制备微球的方法

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EP1385488A2 (fr) 2000-12-07 2004-02-04 President And Fellows Of Harvard College Procedes et compositions utiles pour encapsuler des agents actifs
US7556776B2 (en) 2005-09-08 2009-07-07 President And Fellows Of Harvard College Microfluidic manipulation of fluids and reactions
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