MICROPARTICLES FOR MAGNETIC HYPERTHERMIA
20240041784 ยท 2024-02-08
Inventors
Cpc classification
B82Y25/00
PERFORMING OPERATIONS; TRANSPORTING
A61N1/406
HUMAN NECESSITIES
A61K41/0052
HUMAN NECESSITIES
International classification
A61K9/50
HUMAN NECESSITIES
A61K41/00
HUMAN NECESSITIES
Abstract
There is provided a microparticle comprising magnetic nanoparticles within a matrix such as a polymer sphere, wherein the magnetic nanoparticles have an anisotropy constant K in the range 1.0 to 3.0?10.sup.5 ergs cm.sup.?3 and exhibit a hysteresis loop under an alternating magnetic field so as to generate hysteresis heating whilst fixed within the polymer sphere. The alternating magnetic field has a maximum field strength in the range 100 to 400 Oe and a frequency in the range 25 kHz to 500 kHz. The magnetic nanoparticles have an axial ratio of at least 1.1 and are preferably magnetite and substantially crystalline. A method of synthesising such magnetic nanoparticles is also provided.
Claims
1. A microparticle comprising magnetic nanoparticles within a matrix, wherein the magnetic nanoparticles have an anisotropy constant K in the range 1.0 to 3.0?10.sup.5 ergs cm.sup.?3 and exhibit a hysteresis loop under an alternating magnetic field.
2. A microparticle according to claim 1, wherein the alternating magnetic field has a maximum field strength in the range 100 to 400 Oe.
3. A microparticle according to claim 1, wherein the alternating magnetic field has a frequency in the range 25 kHz to 500 kHz.
4. A microparticle according to claim 1, wherein the magnetic nanoparticles have a median diameter between 8 to 30 nm.
5. A microparticle according to claim 1, wherein the magnetic nanoparticles have a standard deviation of a log normal distribution volume between 0.2 and 0.5.
6. A microparticle according to claim 1, wherein the magnetic nanoparticles have an axial ratio of at least 1.1.
7. A microparticle according to claim 1, wherein the matrix is an organic matrix, or a ceramic matrix or an inorganic matrix.
8. A microparticle according to claim 1, wherein the matrix contains 20 to 60 wt. % and more preferably 40 to 60 wt. % magnetic nanoparticles relative to the weight of the matrix.
9. A microparticle according to claim 1, wherein the magnetic nanoparticles comprise a magnetic material formed from at least one divalent transition metal X, where X is one of the group of Fe, Co, Ni, Mn, Ba, Sr.
10. A microparticle according to claim 1, wherein the magnetic nanoparticles are magnetite nanoparticles.
11. A microparticle according to claim 10, wherein the magnetite nanoparticles are substantially crystalline.
12. A microparticle according to claim 1, wherein the matrix is formed as a sphere, preferably having a diameter in the range 0.1 ?m to 20 ?m, and more preferably in the range 0.1 ?m to 10 ?m.
13. A microparticle according to claim 12, wherein the diameter of the sphere is selected to ensure that in use the inverse of the relaxation time ?.sub.B of the sphere is greater than an applied magnetic field frequency.
14. A microparticle according to claim 1, wherein the matrix is a polymer sphere.
15. A microparticle according to claim 14, wherein the polymer sphere is formed from one of the group consisting of polystyrene, poly(methyl methacrylate), or any biocompatible polymer such as poly(vinyl acetate), poly(vinyl chloride), divinylbenzene.
16. A method of synthesising magnetic particles comprising disposing magnetic nanoparticles comprising a magnetic material formed from at least one divalent transition metal X, where X is one of the group of Fe, Co, Ni, Mn, Ba, Sr in an alkali solution, gradually adding an X II salt solution to create a growth mixture, heating the growth mixture and cooling to create modified magnetic nanoparticles with an anisotropy constant K in the range 1.0 to 3.0?10.sup.5 ergs cm.sup.?3.
17. A method of synthesising magnetic particles according to claim 16, wherein the magnetic nanoparticles are exposed to the growth mixture until the magnetic nanoparticles grow to reach an axial ratio of at least 1.1.
18. A method of synthesising magnetic particles according to claim 16, wherein the growth mixture is heated to around 100? C. for around 1 hour.
19. A method of synthesising magnetic particles according to claim 16, wherein the modified magnetic nanoparticles are encapsulated into polymer microspheres.
20. A method of synthesising magnetic particles according to claim 16, wherein the magnetic nanoparticles are magnetite nanoparticles and the salt solution is an Fe II salt solution.
21. Magnetic particles as formed in accordance with claim 16.
Description
[0019] The invention will now be described, by way of example, with reference to the accompanying drawings in which:
[0020]
[0021]
[0022]
[0023]
[0024]
[0025]
[0026]
[0027]
[0028]
DESCRIPTION
[0029] When a colloid containing individual magnetic nanoparticles is exposed to an applied AC magnetic field, the magnetic nanoparticles dispersed in the liquid respond to the magnetic field to generate heating through susceptibility loss, hysteresis heating and also stirring as shown in
[0030] where t is the time of measurement, kB Boltzmann's constant, T is the temperature of measurement, f is 10.sup.9 s.sup.?1, and K is the anisotropy constant.
[0031] Heating through hysteresis losses occurs in region 12 and above a certain diameter D.sub.p(H) which is dependent on the applied field amplitude, particles will not contribute to either susceptibility or hysteresis loss heating and only viscous heating due to stirring of the particles within the colloid will occur, region 14. This effect becomes more pronounced as particles aggregate and can lead to very high temperatures in the colloid. D.sub.p(H) is given by:
[0032] where M.sub.s is the saturation magnetisation and H is the magnetic field amplitude.
[0033] For magnetite nanoparticles having a diameter D.sub.p(0)<D<D.sub.p(H), only hysteresis loss heating will occur arising from the energy released as a magnetic material is cycled around its hysteresis loop by an AC magnetic field.
[0034] For controllable magnetic hyperthermia, quantifiable and predictable heating is required which cannot be achieved from individual magnetic nanoparticles dispersed in a liquid, such as water or blood. By immobilising magnetic nanoparticles within microspheres, with the magnetite nanoparticles dispersed throughout a matrix forming the microsphere, the magnetic nanoparticles cannot move relative to one another under the influence of an alternating magnetic field. By fixing the magnetic nanoparticles in position, they cannot physically rotate and generate uncontrollable and unpredictable heat by viscous drag.
[0035] By selecting the size distribution of magnetic nanoparticles and immobilising the magnetic nanoparticles within a matrix, so as to only generate heating through hysteresis heating, the heating effect is reduced by approximately 40% over unconstrained magnetic nanoparticles in a liquid.
[0036] The amount of heat generated from hysteresis heating P.sub.h is proportional to the frequency (f) multiplied by the area of the hysteresis loop, given by:
P.sub.h=2M.sub.sf ?.sub.v.sub.
[0037] where V.sub.p(H) is the volume of a particle having a diameter D.sub.p(H), H.sub.c is the coercivity and f(V) is the distribution of physical volumes.
[0038] The anisotropy constant of the magnetic nanoparticles and the applied field affects the hysteresis heating. With conventional spherical magnetite nanoparticles, the anisotropy constant K is less than 1?10.sup.5 ergs cm.sup.?3 which results in minimal hysteresis heating regardless of the field applied. The modified magnetic nanoparticles of the present invention are formed with an elongated shape as discussed in detail below so as to have an increased anisotropy constant, typically with the anisotropy constant K in the range 1.0 to 3.0?10.sup.5 ergs cm.sup.?3. This greatly increases the hysteresis heating able to take place at applied fields of 100 to 400 Oe.
[0039]
[0040]
[0041] Using such data allows the hysteresis heating generated to be calculated using equation 3 and controlled. The degree of hysteresis heating required can be configured by choosing particles with the required anisotropy constant and selecting the magnetic field strength and frequency known to give appropriate hysteresis heating for that anisotropy constant. A lower operating frequency provides a greater degree of control over the heating exhibited by the immobilised modified magnetite nanoparticles and by selecting a field amplitude in the range 150 Oe to 400 Oe substantially the whole of the magnetic particle size distribution will generate hysteresis heating.
[0042] The preparation of the modified elongate magnetite nanoparticles with an anisotropy constant
[0043] K in the range 1.0 to 3.0?10.sup.5 ergs cm.sup.?3 will now be described.
[0044] The standard method for the preparation of magnetite nanoparticles is the co-precipitation process of Khalafalla and Riemers, see U.S. Pat. No. 3,843,540. This gives nanoparticles of diameter 10 nm or less which are too small to give significant hysteresis. To produce magnetite nanoparticles with an increased anisotropy constant and which are suitable for magnetic hyperthermia via hysteresis, an alternative growth method has been derived.
[0045] Thus in accordance with one aspect of the invention, the preparation of suitable magnetite nanoparticles for magnetic hyperthermia proceeds in two stages. The first stage is the standard co-precipitation method for the production of magnetite nanoparticles of Khalafalla and Riemers as above. The detailed example below uses a combination of Iron II Chloride and Iron III Chloride salts dissolved in water. Those of skill in the art will also know that other combinations of Iron II and Iron III salts can also be used with the appropriate molar ratio. The chlorides dissolved in water are then combined with a concentrated solution of sodium hydroxide (NaOH) via a peristaltic pump. Those of relevant skill in the art will be aware that other hydroxides such as potassium hydroxide (KOH) or ammonia (NH.sub.3OH) or any other suitable hydroxide can also be used. This co-precipitation process produces spherical magnetite nanoparticles with a median diameter ranging between 8 and 11 nm.
[0046] The second stage of preparation involves exposing the magnetite nanoparticles to a growth layer solution such as FeCl.sub.2 to deposit additional Iron II onto the particles formed by the co-precipitation method. This increases the diameter of the particles with the growth process acting to elongate the particles so they are no longer spherical and become spheroid, so increasing their anisotropy constant. Following these two stages the modified elongate magnetite nanoparticles are then thoroughly washed and re-introduced to a solution of concentrated alkali where any of the alkalis above can be used. A solution of Iron II Chloride (FeCl.sub.2) is then added at a constant rate with further stirring and heating for a period of one hour at 100? C. Other rates of addition and other similar heating regimes for varying times can be used. Those of skill in the art will also be aware that other Iron II compounds such as iron sulphate could also be used for this additional growth process.
EXAMPLE
[0047] A detailed example of preparation of microparticles configured for hyperthermia using the two stage controlled growth process is as follows.
First Stage: Co-Precipitation
[0048] An Iron III salt such as FeCl.sub.3.6H.sub.2) (142.6 g, 0.527 mol) was dissolved in distilled water giving a total volume of 400 ml. A second solution of an Iron II salt such as FeCl.sub.24H.sub.2O (111.2 g, mol) was dissolved in distilled water giving a total volume of 400 ml. The two solutions were then combined and mixed with an overhead stirrer at 500 rpm for 5 minutes. A 10M NaOH aqueous solution (580 ml, 5.8 moles) was then added via peristaltic pump at a rate of 1700 ml/min to the Fe II/III salt solution producing a black precipitate.
[0049] Once the addition of the NaOH solution was completed stirring was continued for 10 minutes before the resulting magnetite nanoparticles were washed in water two times. Distilled water was added bringing the mass of magnetite slurry to 1000 g, the magnetite nanoparticles having a median diameter between 8 and 11 nm.
Second Stage: Preparation of Growth Layer
[0050] To achieve deposition of a growth layer on the magnetite nanoparticles and so create modified magnetite nanoparticles, for this example with a median diameter of 12.3 nm, an alkali solution such as 10M NaOH aqueous solution (15 ml, 0.15 moles) was added to the magnetite slurry and pH checked to confirm pH =12. The slurry was stirred with an overhead stirrer at 500 rpm for 5 minutes.
[0051] To create a growth layer solution, an Iron II salt such as FeCl.sub.2.4H.sub.2O (12.92 g, 0.065 mol) was dissolved in distilled water giving a total volume of 65 ml (1.0 M solution). To achieve thicker growth layers, the concentration of FeCl.sub.2 is increased and for example to achieve modified magnetite particles with a median diameter of 15.4 nm after growth, FeCl.sub.2.4H.sub.2O (51.69 g, 0.260 mol) was dissolved in distilled water giving a total volume of 260 ml (1.0 M solution).
[0052] Stirrer speed was reduced to 250 rpm and the growth layer FeCl.sub.2 solution was added via peristaltic pump at a rate of 250 ml/min. Slurry was stirred at 250 rpm at room temperature for one hour before being heated to 100C and stirred for one hour. The resultant slurry was allowed to cool and washed with six times with tap water until pH=8. The magnetite nanoparticles within the slurry are now modified in shape being elongate with an axial ratio of at least 1.1 and typically in the range 1.1 to 2.2. The addition of the extra Fe II using the growth layer solution restores the Fe3+ rich magnetite particle surface back closer to the ideal Fe3+/Fe2+ ratio of 2:1. This increases the saturation magnetisation M s from about 70 emu/g to about 80 emu/g. As shape anisotropy constant varies with M.sub.s.sup.2, this increases K by about 30% with further increase in K due to elongation of the particles during the growth process.
[0053] Typically the median diameter of the modified magnetite nanoparticles is greater than 8 nm and less than or equal to 30 nm. The elongate magnetite nanoparticles resulting from the growth process have an anisotropy constant K in the range of 1.0 to 3.0?10.sup.5 ergs cm.sup.?3 so as to exhibit a hysteresis loop under an applied field in the range 100 Oe to 400 Oe. Small variations will occur in anisotropy constant within any batch of particles obtained from the growth process due to variation in particle size within any such batch as is shown in
[0054] The modified magnetite Fe.sub.3O.sub.4 particles produced by the controlled growth process are shown in
[0055] The diameter of the modified particles is measured using transmission electron microscopy and the modified particles have a median diameter in the range 8 nm to 30 nm with a standard deviation of a lognormal distribution volume of between 0.2 and 0.5 as shown in
[0056] Unmodified magnetite nanoparticles are shown for comparison in
[0057] After the first two stages are completed, the modified particles are coated with oleic acid to enable the modified magnetite nanoparticles to be separated from the slurry. Thus water (300 ml) and 35% Ammonia solution (20 ml, 0.36 moles) are added to the slurry followed by oleic acid (30 ml). This coating mixture was stirred with an overhead stirrer at 600 rpm for one hour. M HCl was then added to the stirring suspension until pH=4.0 when the coated particles separate from the slurry and the coated modified magnetite particles washed.
[0058] The modified magnetite nanoparticles resulting from the growth process were then encapsulated into a matrix to create microparticles useable in hyperthermia. The matrix can be an organic matrix such as provided by polymer or other plastics material, or a ceramic matrix or an inorganic matrix which may or may not be biodegradeable. There are many methods for the production of microparticles or microbeads known to those of ordinary skill in the art. Here by way of example only, one such process is described.
[0059] To prepare polymer microspheres encapsulating modified magnetite nanoparticles, 7.5 g Crodafos 0.5 A with 35.0 g styrene monomer was mixed in a beaker with 2 g of modified magnetite particles synthesised using the growth process as aforesaid and then mixed with a rotor stator mixer for 15 minutes. The resulting mixture was then subjected to a high energy ultrasonic disintegration for a further 30 minutes to disperse particles using a Soniprep? 150. 30 g of the styrene-based ferrofluid was then added to the water phase (10% styrene in water) and dispersed using an ultrasonic disintegrator for 10 minutes to generate an emulsion. 0.3 g of water-soluble initiator, for example Potassium Persulphate K.sub.2(SO.sub.4).sub.2, was then added to the emulsion.
[0060] After this, the prepared emulsion was then loaded into a 500 ml three necked flask fitted with stirrer, condenser and nitrogen inlet for polymerisation (step 1). The emulsion was stirred at rpm for 5 mins under a flow of nitrogen (step 2). The temperature was then raised to 70? C. and kept at 70? C. under a flow of nitrogen for 6 hours (step 3), with the solution was allowed to cool under a flow of nitrogen (step 4).
[0061] The solution was then added to a 2.5 litre stainless steel beaker and placed over a magnetic plate to achieve separation (step 5). The solution was topped up to 1 litre with 0.5 wt % sodium dodecyl sulphate, stirred and re-separated on a magnet (step 6). The supernatant liquid was decanted (step 7). The remaining polymer microspheres containing the modified magnetite nanoparticles were then washed several times in deionised water.
[0062] Thus elongate magnetite nanoparticles with an anisotropy constant K in the range 1.0 to 3.0?10.sup.5 ergs cm.sup.?3 are encapsulated into a matrix, typically a plastics material matrix achieved by emulsion polymerisation, to create polymer microspheres sterile for in vivo use which range in size from 0.1 ?m to 20 ?m, and more preferably from 0.1 ?m to 10 ?m. The volumetric loading of the magnetite within the polymer spheres is typically in the range 20 to 60% by weight, and more preferably 40 to 60% by weight, and is sufficient to ensure the microparticles exhibit hysteresis heating. The polymer microspheres can be functionalised with external markers so as to attach to cancer cells. In addition to prove the efficiency of the microspheres in tumour reduction, the surface of the microspheres can be functionalised with drugs such as doxyrubicin or cancer cell inhibitors such as the synthetic peptide Nucant.
[0063] The resulting microspheres are of further benefit as such spheres, having a diameter in the range of 0.1 ?m to 20 ?m encapsulating magnetic nanoparticles with an anisotropy constant K in the range 1.0 to 3.0?10.sup.5 ergs cm.sup.?3 so as to exhibit a hysteresis loop under an alternating magnetic field, have a Brownian relaxation time sufficient to ensure that individual microspheres cannot rotate in an AC field even when magnetic nanoparticles within the sphere are fully magnetised. This ensures that any heating is from hysteresis heating alone without any residual effects from movement or clustering of the microspheres.
[0064] The rotation time of a microsphere in a liquid is determined by the Brownian relaxation time (?.sub.B) given by
(?.sub.B=3V.sub.H?/k.sub.BT) Equation 4
where V.sub.H is the hydrodynamic volume of the particle, ? the viscosity of the liquid environment, kB is Boltzmann's constant and T is the temperature. By encapsulating the individual magnetic particles within a polymer sphere that is much larger than the magnetic particles, the time for the polymer sphere to rotate as the magnetic field changes direction becomes much greater than the switching time of the AC magnetic field. Stirring by movement of the microparticles themselves cannot take place in response to the alternating magnetic field. This is shown in
[0065] As the magnetic nanoparticles are encapsulated within a larger micro-sized particle, namely the polymer microsphere itself, heating due to rotation and thus stirring by the microsphere is eliminated as the microsphere itself has no permanent net magnetic moment and the rotation time for such a microsphere is greater than the switching time of the alternating magnetic field.
[0066]
[0067] where C is the specific heat of the colloid, ? is its density and ? is the concentration of elemental iron (Fe) in the colloid. AT is the rise in temperature in a time ?t. Measuring the SAR of the magnetite nanoparticles when encapsulated in polymer spheres gave a SAR for hysteresis heating of 28.4 W/g.
[0068]
[0069] Thus magnetic nanoparticles can be synthesised using a growth process as aforesaid to have an anisotropy constant K of between 1.0 to 3.0?10.sup.5 ergs cm.sup.?3. When encapsulated in polymer microspheres and exposed to a magnetic field in the range of 100 to 400 Oe and a field frequency in the range of 25 kHz to 500 kHz, localised hysteresis heating can be achieved, with such magnetic hyperthermia useful for treating tumours.