Patent Application
20240009329
The present invention concerns freeze-dried microbubbles, their method of preparation, as well as their use, in particular as contrast agents.
Microbubbles find use in numerous applications such as molecular imaging, non-invasive blood pressure measurements, drug delivery, sonoporation and biosensors (Segers et. al, RSC Nanoscience and Nanotechnology, 2015, p. 81-101).
For many of these applications, microbubbles having a diameter between 0.5 and 10 μm and having a low polydispersity index are desired, in particular having a polydispersity index below 10%. In clinical applications, a polydisperse set of microbubbles can present several disadvantages:
In addition, since these microbubbles are susceptible to be used in a clinical environment, they should be physiologically inert, and exempt of toxic constituents, such as residual solvents. Furthermore, because the microbubbles might not be used immediately after production, they should be stored in a convenient and sufficiently stable form, preferably as a freeze-dried powder.
In this respect, the microbubbles that exist today, in particular commercialized microbubbles, do not meet the above-mentioned standards. Indeed, commercialized and clinically approved microbubbles are polydisperse and are sold in a freeze-dried form, while some other today's bubbles either contain solvents toxic to the patient, or are sold in a non-freeze-dried form.
For clinical uses, freeze-dried products are advantageous over non-freeze-dried products, because freeze-drying confers interesting properties to the products, as compared to products which are not freeze-dried. For example, freeze-dried products are expected to have improved stability, improved bioavailability and improved dissolution kinetics. Furthermore, residual solvents used during synthesis are more efficiently removed by freeze-drying than by conventional drying methods.
Freeze-dried mono-disperse microbubbles are difficult, if not impossible to obtain, because the freeze-drying procedure leads to loss of monodispersity, leading to a final product that is polydisperse.
Thus, one aim of the present invention is to provide freeze-dried monodisperse microbubbles. Another aim of the present invention is to provide a process for the preparation of monodisperse freeze-dried microbubbles.
Another aim of the invention is to provide monodisperse microbubbles that are stable upon storage for prolonged periods, in particular more than 1 year at room temperature.
Yet another aim of the present invention is a process of resuspension of freeze-dried monodisperse microbubbles, in particular using microfluidic techniques.
Yet another aim of the present invention is to provide a suspension of monodisperse freeze-dried microbubbles.
A further aim of the present invention is the use of freeze-dried monodisperse microbubbles, in particular as contrast agents, due to their excellent echogenic properties.
Yet another aim of the present invention is the provision of a microfluidic chip comprising freeze-dried monodisperse microbubbles.
Thus, a first object of the present invention is freeze-dried monodisperse microbubbles, wherein:
The invention also pertains to at least one freeze-dried monolayer of monodisperse microbubbles adsorbed on a hydrophilic surface,
wherein the microbubbles:
The invention also pertains to a hydrophilic surface comprising at least one monolayer of freeze-dried monodisperse microbubbles, wherein the microbubbles:
In what follows, “freeze-dried monodisperse microbubbles adsorbed on a hydrophilic surface in the form of at least one monolayer” has the same meaning as “at least one freeze-dried monolayer of monodisperse microbubbles adsorbed on a hydrophilic surface”
The inventors have surprisingly found that arranging monodisperse microbubbles on a hydrophilic surface, in the form of at least one monolayer, allows for subsequent freeze-drying of the microbubbles, and further resuspension, without the loss of the monodispersity and without substantial change in the value of the polydispersity index.
Without being bound to theory, when the microbubbles are arranged in a monolayer, the interactions, such as electrostatic interaction, between the microbubbles are limited as compared to the interactions between microbubbles in the form of a bulk powder, not arranged in a monolayer. These reduced interactions stabilize the microbubbles, making them less sensitive towards the potentially destructive action of freeze-drying.
For the sake of comparison, when the microbubbles are arranged in a multilayer, instead of a monolayer, the monodispersity is degraded, in particular by the phenomena of coalescence and Ostwald ripening, even before freeze-drying, even when the microbubbles are immediately transferred into the freezer.
This innovative approach of providing at least one monolayer of microbubbles, which according to the inventors has no precedent, allows access to monodisperse freeze-fried microbubbles as well as monodisperse resuspended microbubbles hereafter designated by “a suspension of microbubbles”.
By “monodisperse” is meant that for a plurality of microbubbles (e.g. at least 100, more preferably at least 1000) the microbubbles have a polydispersity index, or coefficient of variation (CV) of their diameters of less than 10%.
The “polydispersity index”, or PDI, represents a measure of the size distribution of the microbubbles. The polydispersity index according to the present invention is calculated according to Formula 1.
in which
d represents the diameter of the individual microbubbles as measured by optical microscopy.
<d> represents the arithmetic average of the measured diameters for a population of microbubbles.
With the expression “below 10%” relating to the polydispersity index, should also be understood the following values: below 9%, below 8%, below 7%, below 6%, below 5%, below 4%, below 3%, and below 2%, in particular the following ranges: from 1 to 10%, 1 to 9%, 1 to 8%, 1 to 7%, 1 to 6%, 1 to 5%, 1 to 4%, 1 to 3%, 1 to 2%, 2 to 9%, 3 to 8%, 4 to 7%, 5 to 6%, 2 to 10%, 3 to 10%, 4 to 10%, 5 to 10%, 6 to 10%, 7 to 10%, 8 to 10%, and 9 to 10%.
The expression “microbubble size” according to the invention is defined as the diameter of the microbubbles as measured by optical microscopy. The diameter is considered starting from the center of the bubble and tracing a straight line to both opposite sides of the shell of the microbubbles. The diameter corresponds to the distance between the extremities of this line, that is to say, the distance between the two opposite points on the interior side of the shell. The bubble size is determined as the arithmetic average of the bubble sizes as measured for a minimum of 100 microbubbles.
With the expression “200 nm to 50 μm” relating to the bubble size, should also be understood the following ranges: 200 to 500 nm, 200 to 750 nm, 200 nm to 1 μm, 200 nm to 5 μm, 200 nm to 10 μm, 200 nm to 20 μm, 200 nm to 30 μm, 200 nm to 40 μm, 500 nm to 50 μm, 750 nm to 50 μm, 1 to 50 μm, 5 to 50 μm, 10 to 50 μm, 20 to 50 μm, 30 to 50 μm, 40 to 50 μm, 500 nm to 40 μm, 1 to 30 μm, and 10 to 20 μm.
The microbubble size is in particular about 5 μm.
The term “monolayer”, within the context of the present invention, refers to a single layer of microbubbles on a hydrophilic surface. Each individual bubble is adjacent to at least another bubble present in the monolayer. Depending on the size of the microbubbles, each individual microbubble in the monolayer might, or might not, touch, or be in contact, with an adjacent microbubble. Thus, microbubbles having a size of 20 to 50 μm comprised in a monolayer are arranged in a “closely packed” configuration. (similar to the one shown in
In contrast, in the case of 5 μm microbubbles as shown in
According to the present invention, “at least one monolayer” refers to one or more than one, monolayer(s) being present on the hydrophilic surface, each individual monolayer being adsorbed onto said surface. Multiple monolayers are thus not stacked on top of each other to form a multilayer, but each monolayer is adjacent, but non-contiguous, to at least one other monolayer.
In this respect, the expression “non-contiguous” signifies that the boundaries of monolayers do not touch to the boundaries of other monolayers present on the hydrophilic surface. In other words, there are no contact points between the outer surface of the shells of the microbubbles present in one monolayer, and the outer surface of the shells of the microbubbles present in another monolayer.
The expression “adjacent” signifies “being next to”.
The different monolayers adsorbed on the hydrophilic surface are thus distributed on the hydrophilic surface and separated from each other by spaces not comprising microbubbles. Typically, and as a non-limiting example, for a hydrophilic surface having dimensions of 25×mm, comprising around 300 monolayers of approximately 1 mm2, the shortest distance between two adjacent monolayers is at least 500 μm to 1 mm.
Thus, according to a preferred embodiment, each monolayer of microbubbles that is present on the hydrophilic surface is separated from an adjacent monolayer by a distance of at least 10 times, preferably at least 20 times, the average size of the microbubbles comprised within the monolayers.
In other words, each individual monolayer macroscopically represents a “spot” comprising an increased concentration of microbubbles as compared to regions not comprising a monolayer. This feature is illustrated in
In what follows, the expressions “monolayer” and “spot” are used, but have the same meaning.
The term “adsorbed” refers to the situation where the microbubbles are attached to the hydrophilic surface through relatively weak interactions, such as electrostatic interactions, or van der Waals forces. For clarity, adsorption does not involve covalent bonding of the microbubbles to the hydrophilic surface.
In a preferred embodiment, the microbubbles are, in addition to being adsorbed to the hydrophilic surface, embedded in a film formed by the shell material.
Thus, an advantageous embodiment of the invention is freeze-dried monodisperse microbubbles, wherein:
In this embodiment, the spaces separating the individual microbubbles comprised within each monolayer, are covered with a film formed by the shell material. Thus, in each monolayer, the hydrophilic surface is covered by microbubbles and by said shell material.
The different monolayers present on the hydrophilic surface are separated from each other by regions devoid of microbubbles and devoid of said film of shell materials. In other words, the different monolayers are separated by regions wherein the hydrophilic surface is exposed to the external environment. As is the case with the microbubbles, the film of shell material is also adsorbed to the hydrophilic surface, through non-covalent interactions.
This embodiment is illustrated by
By “core” is meant the volume inside the microbubble, delimited by the inner surface of the shell and comprised of a specific material, different from the shell material. The core being surrounded by the shell. With respect to the microbubbles according to the present invention, the core material comprising the core is a gaz.
By “shell” is meant the material completely surrounding the core.
The expression “physiologically inert” refers to a material or chemical component that does not produce an adverse physiological reaction when administered to a subject, or a patient. Adverse physiological reactions include, for example, allergic and other systemic reactions, or local inflammation and toxicity. In particular, the microbubbles according to the present invention show a low risk of adverse reactions, occurring in less than 1% of the patients, and when adverse reactions do occur, they tend to be mild.
The freeze-dried monodisperse microbubbles of the invention, as well as the suspension of the invention, are stable.
Thus, in another embodiment of the invention, the freeze-dried monodisperse microbubbles, in the form of at least one monolayer, are stable for at least six 6 months when stored at room temperature in air, in particular for at least 12 months, or are stable for at least 12 months at 4° C., in particular for at least 16 months.
Under these conditions less than 10%, or less than 5%, in particular less than 1%, of the microbubbles lose their ability to be used as a contrast agent.
In another embodiment of the invention, the shell of the freeze-dried monodisperse microbubbles, in the form of at least one monolayer, is permeable to gaz.
Under vacuum, in particular at pressures below 10 mbar, the gas comprised in the core of the microbubbles can diffuse through the shell and exit the microbubbles. Alternatively, when placed in an external environment comprising a different gas than the one comprised in the core, an exchange of gazes can occur, whereby the gas of the external environment substitutes the gas of the core.
Thus, when microbubbles bubbles comprising PFC in the core, are placed in solutions saturated in air, the air can enter the core through the gas-permeable shells faster than PFC leaves the core, because PFC/SF6 is heavier than air, leading to increased internal pressure in the bubble which can lead to the microbubbles to dilate.
In contrast, if the PFC loaded microbubbles are placed in a gas deficient environment, such as blood, the gas from the core can diffuse out and the microbubble can dissolve in the environment in which it is comprised. This is useful in vivo, because it prevents capillary blockage. Then, escaped, dissolved, gas is eliminated from the body through exhaled breath by the lungs (S. Podell et. al., Physical and biochemical stability of Optison®, an injectable ultrasound contrast agent, Biotechnol. Appl. Biochem. (1999) 30, 213-223).
In another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the shell of the microbubbles has a thickness of from 50 to 100 nm, as measured by scanning electron microscopy.
With the expression “50 to 100 nm” is also meant the following ranges: 50 to 90 nm, 50 to 80 nm, 50 to 70 nm, 50 to 60 nm, 60 to 100 nm, 70 to 100 nm, 80 to 100 nm, 90 to 100 nm, 55 to nm, 60 to 80 nm and 65 to 75 nm.
The present invention also relates to freeze-dried monodisperse microbubbles, wherein:
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the shell of the microbubbles comprises, or consists of:
The expression “amphiphilic polymer” is understood to mean a polymer which comprises at least one hydrophilic part and at least one hydrophobic part.
The expression “water-soluble proteins” refers to proteins having an aqueous solubility at 25° C. of more than 10 g/L, more in particular more than 40 g/L.
The expression “cryoprotectant” refers to a compound used to protect the microbubbles from physical or chemical decay during freezing. Without being bound to theory, the cryoprotectant forms a solid coating that protects the microbubbles from ice crystals that can form during freezing, and from forces associated with exposing the microbubbles to high vacuum during freeze-drying.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the amphiphilic polymer is both the surfactant and the cryoprotectant.
According to this embodiment, the surfactant present in the shell also has cryoprotecting properties. This is for example, and in particular, the case for the polymer “polyvinyl alcohol”, or “PVA”. In this situation, an additional surfactant, or an additional cryoprotectant is not necessarily, but can be present in the shell.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the amphiphilic polymer is a water-soluble amphiphilic polymer chosen from the group consisting of:
polyvinyl alcohol (PVA), polyvinylpyrrolidone (PVP), poly(lactic-co-glycolic acid) (PLGA) and chitosan,
or mixtures of said amphiphilic polymers,
the amphiphilic polymer preferably being polyvinyl alcohol.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the water-soluble protein is serum albumin.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the phospholipid is chosen from the group consisting of:
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the cryoprotectant is chosen from the group consisting of:
Examples of sugars that can be used in the present invention are trehalose, sucrose, glucose, and fructose.
In yet another embodiment, when the microbubbles are embedded in a film formed by the shell material, the shell material is present in the shell of the microbubbles at a ratio of approximately 1:200000 w/w with respect to the total weight of the shell material comprised in the film and in the shell of the microbubbles.
In this embodiment, ratio refers to the cumulative weight of shell materials comprised in the sum of all microbubbles present in a monolayer, compared to all the shell material comprised in the monolayer, both in the film and in the shells. With “approximately 1:200000” is meant a value comprised from 100:200000 to 1:100000
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the core of the microbubbles comprises or consists of a gas.
The gas comprised in the core is preferably a hydrophobic gas, in particular a gas chosen from: air, SF6, or perfluorinated hydrocarbons, or mixtures of these gases, in particular perfluorohexane, or a mixture of perfluorohexane and SF6.
In yet another embodiment, the invention relates to freeze-dried monodisperse microbubbles as previously described, wherein the shell of the microbubbles comprises, or consists of:
In yet another embodiment, the invention relates to freeze-dried monodisperse microbubbles as previously described, wherein the amphiphilic polymer is a water-soluble amphiphilic polymer chosen from the group consisting of:
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the hydrophilic surface is a glass surface, in particular a sodium silicate, or boro silicate glass surface.
The hydrophilic glass surface is preferably pre-treated with O2 μlasma to ensure a clean, etched glass surface to which the microbubbles are adsorbed in an optimal manner.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the hydrophilic surface is flat or curbed, preferably flat, in particular a flat glass slide.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the microbubbles are adsorbed on a hydrophilic surface in the form of a single monolayer, said monolayer being continuous, uninterrupted by regions that are devoid of microbubbles.
In this embodiment, a single monolayer is present on the hydrophilic surface, without the presence of multiple spots. The microbubbles can be embedded in a film of shell material, adsorbed to the hydrophilic surface.
Typically, as a non-limiting example, such a single monolayer, adsorbed on a hydrophilic surface having the dimensions of 25×75 mm can comprise from 2 to 106 individual microbubbles depending on the size of each microbubble. Preferably the monolayer comprises about 106 individual microbubbles.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the microbubbles are adsorbed on a hydrophilic surface in the form of more than one monolayers, in particular of from 2 to 1000 monolayers, preferably about 100 monolayers, said more than one monolayers being non-contiguous with respect to each other.
In this embodiment, multiple monolayers of microbubbles are present on the hydrophilic surface, in the form of spots.
With the expression “of from 2 to 1000 monolayers” is also meant the following ranges: of from 2 to 800, 2 to 600, 2 to 400, 2 to 200, 2 to 100, 2 to 50, 2 to 10, 10 to 1000, 50 to 1000, 100 to 1000, 200 to 1000, 400 to 1000, 600 to 1000, 800 to 1000, 50 to 900, 100 to 800, 200 to 600, 300 to 500.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the distance between a first monolayer and a second monolayer, adjacent and non-contiguous to the first monolayer, is substantially identical to the distance between any one of two adjacent non-contiguous monolayers on the hydrophilic surface.
In this embodiment, the distances between each adjacent monolayer adsorbed to the hydrophilic surface are substantially the same. In other words, the plurality of monolayers are homogeneously distributed on the hydrophilic surface,
wherein said distance is the closest distance between the boundaries of the first and the second monolayer.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the microbubbles are adsorbed on a hydrophilic surface in the form of at least 100 monolayers, and wherein the hydrophilic surface has a dimension of approximately 25 by 75 mm.
Typically, as an example, in a configuration wherein 100 monolayers are adsorbed to a hydrophilic surface having the dimensions of 25×75 mm, wherein each monolayer in particular comprises from 1 to 104 individual microbubbles. Thus, in this example, a total of about 106 microbubbles is present on the surface, the amount needed for clinical use in applications of the microbubbles as contrast agents.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein each of the monolayer(s) comprises of from 2 to 106 microbubbles, in particular approximately 104 microbubbles.
In yet another embodiment, the present invention concerns freeze-dried monodisperse microbubbles as previously described, wherein the microbubbles are adsorbed on a hydrophilic surface in the form of a single monolayer, said monolayer being continuous, uninterrupted by regions that are devoid of microbubbles,
or wherein the microbubbles are adsorbed on a hydrophilic surface in the form of more than one monolayers, in particular of from 2 to 1000 monolayers, preferably about 100 monolayers, said more than one monolayers being non-contiguous with respect to each other,
in particular wherein the distance between a first monolayer and a second monolayer, adjacent and non-contiguous to the first monolayer, is substantially identical to the distance between any one of two adjacent non-contiguous monolayers on the hydrophilic surface.
The invention also concerns a hydrophilic surface comprising at least one monolayer of freeze-dried monodisperse microbubbles,
wherein the microbubbles and the hydrophilic surface are as previously defined.
The invention also concerns a hydrophilic surface comprising at least one monolayer of freeze-dried monodisperse microbubbles,
wherein the microbubbles and the hydrophilic surface are as previously defined.
The invention also concerns a freeze-dried monolayer of monodisperse microbubbles adsorbed on a hydrophilic surface,
wherein the microbubbles and the hydrophilic surface are as previously defined.
A second object of the present invention relates to freeze-dried monodisperse microbubbles in the form of a powder, wherein:
According to this embodiment of the invention, the freeze-dried microbubbles are not adsorbed to a hydrophilic surface in the form of a monolayer but exist in the form of a bulk powder consisting of microbubbles.
With the expression “substantially devoid of organic solvents” is meant that the microbubbles comprise less than 500 ppm of organic solvent, in particular less than 250 ppm, 100 ppm, 50 ppm, 25 ppm, 10 ppm, preferably less than 1 ppm.
By “organic solvents” should be understood solvents, other than the gas comprised in the core of the microbubbles. These organic solvents are typically present as residual solvents resulting from the process by which the microbubbles are prepared. For instance, when using an emulsion-based microbubbles preparation method, an aqueous phase and an organic solvent are used, the result of which is that residual organic solvents can end up in the microbubbles.
Class 1 and/or class 2 refers to the ICG Q3C (R6) guidelines of the European Medicines Agency, version of Aug. 9, 2019, dealing with sets the guidelines for residual solvents present in pharmaceutical ingredients.
In contrast, the microbubbles according to the present invention can be obtained using microfluidic techniques, involving the use of strictly aqueous media.
Thus, a third object of the present invention is a process for preparing freeze-dried microbubbles, wherein the microbubbles:
In other words, the invention pertains to a process for preparing a freeze-dried monolayer of monodisperse microbubbles,
wherein the microbubbles:
The invention also relates to a process for preparing freeze-dried microbubbles, wherein the microbubbles:
Classic freeze-drying techniques, known to the person skilled in the art can be implemented in the process according to the present invention. A shelf freeze-drier is preferably used, wherein the hydrophilic surface can be placed on a tray, or a shelf. The time necessary to freeze-dry is approximately 4 hours but depends on the amount of sample to be freeze-dried.
In another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the process comprises the steps of:
The step of collecting the monodisperse microbubbles on a hydrophilic surface can be carried out by spreading the microbubbles onto the hydrophobic surface. In a typical production process, the tip of the tube from which the microbubbles exit the microfluidic chip, is moved over the hydrophilic surface, allowing the deposition of the microbubbles on said surface (
In case multiple monolayers are to be produced, the tip of the tube from which the microbubbles exit the microfluidic chip is briefly, for example for 1 to 3 seconds, contacted with the hydrophilic surface. Upon contact, a monolayer is deposited. Repeating said contact, on a different place on the hydrophilic surface leads to the deposition of a subsequent monolayer. In a typical non-limiting example, during each contacting, a drop of 0.1 μl, comprising 104 microbubbles, is deposited on the surface. This contacting on a different place on the hydrophilic surface can be achieved either by moving the tip over the hydrophobic surface, or by moving the hydrophilic surface under the tip. During these moving operations, the tip is not in contact with the surface. Each drop, in addition to comprising microbubbles, also comprises residual shell material, in particular cryoprotectant.
Upon freeze-drying, the solvent comprised in the drop is removed, leaving a dried monolayer of microbubbles, and a dried film, or coating of residual shell materials comprised in the drop, on the hydrophilic surface. The result of this is that each at least one monolayer is comprised of microbubbles embedded in a film of freeze-dried shell material.
In another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the process comprises the steps of:
In another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the process further comprises:
before the step of freeze-drying or before the optional step of freezing, a step of
The step of forming monodisperse microbubbles can be performed using standard microfluidic techniques (Introduction to Microfluidics, Patrick Tabeling, Oxford University Press, 2005). A microfluidic flow-focusing geometry such as shown in
In a preferred embodiment, the microbubbles are generated at a frequency of up to 10 kHz, corresponding to a throughput of 6×105 microbubbles per minute.
During freeze-drying, which is performed in vacuum, the gas comprised in the core of the microbubbles might diffuse from the core, due to the gas-permeability of the shell. Then, when the vacuum is removed, gases can rediffuse into the core. Placing the freeze-dried microbubbles in an environment comprising a specific gas, such as air, SF6, or perfluorinated hydrocarbons, or mixtures of these gases, allows for the introduction of this/these gas(es) into the core.
Thus, in a particular embodiment, the process of the present invention further comprises a step of introducing a gas into the core of the microbubbles, wherein the freeze-dried microbubbles are placed in an environment comprising the gas to be introduced in the core.
Thus, when the freeze-dried microbubbles are placed in air, their core, upon removal of the vacuum, fill with air of the environment.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the process further comprises, between the step of collecting and the step of freeze-drying, a step of:
In this embodiment, the microbubbles are frozen prior to the freeze-drying step and after the step of collecting the microbubbles. The collected microbubbles are sufficiently humid to be able to be frozen, along with the residual water.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the step of collecting the monodisperse microbubbles comprises:
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the step of collecting the monodisperse microbubbles comprises:
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the step(s) of contacting said hydrophilic surface with said tip is carried out for a period of 1 to 3 seconds.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the step of collecting the monodisperse microbubbles comprises:
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the step of freezing is carried out at a temperature below the glass transition temperature of the cryoprotectant,
At temperatures below the glass transition temperature of the cryoprotectant, the shell material hardens, offering protection from the destructive action of freezing the microbubbles.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the step of freeze-drying is carried out at a temperature below the glass transition temperature of the cryoprotectant, in particular at a shelf temperature below −40° C., in particular at a temperature of −50° C.
At temperatures below the glass transition temperature of the cryoprotectant, the shell material hardens, offering protection from the destructive action of freeze-drying the microbubbles.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the relative difference in the arithmetic average size of the monodisperse microbubbles before the freezing and/or freeze-drying steps, compared to after the freezing and/or freeze-drying step is less than 20%, preferably less than 10%.
Freezing microbubbles leads to shrinkage of the microbubbles. Thus, frozen, and freeze-dried microbubbles are smaller than the microbubbles as collected before the freezing and/or freeze-drying step.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the relative difference in the polydispersity index of the microbubbles before the freezing and/or freeze-drying steps, compared to after the freezing and/or freeze-drying step is less than 20%, preferably less than 10%.
With the expression “less than 20%”, should also be understood: less than 18%, 16%, 14%, 12%, 10%, 8%, 6%, 4%, 2%, in particular less than 1%.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the shell of the microbubbles has a thickness of from 50 to 100 nm, as measured by scanning electron microscopy.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the liquid phase comprises:
The liquid phase further comprises an aqueous component, in which the surfactant and the cryoprotectant are solubilized.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the amphiphilic polymer is a water-soluble polymer, chosen from the group consisting of:
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the phospholipid is chosen from the group consisting of:
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the cryoprotectant is chosen from the group consisting of:
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the amphiphilic polymer is both a surfactant and/or a cryoprotectant, preferably polyvinyl alcohol.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the gas phase comprises, or consists of a hydrophobic gas, in particular chosen from:
air, SF6, or perfluorinated hydrocarbons, or mixtures of these gases,
in particular perfluorohexane, or a mixture of perfluorohexane and SF6.
Hydrophobic gas in the sense of the invention are gaseous substances that are not freely miscible with water in the liquid phase
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the liquid phase comprises:
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the amphiphilic polymer is a water-soluble amphiphilic polymer chosen from the group consisting of:
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the hydrophilic surface is a glass surface, in particular a sodium silicate, or boro silicate glass surface.
In yet another embodiment, the present invention concerns a process for preparing freeze-dried microbubbles as previously described, wherein the hydrophilic surface is flat or curbed, preferably flat, in particular a glass slide.
The present invention also concerns a process for producing freeze-dried monodisperse microbubbles, in the form of a powder, wherein the process comprises a step of:
The microbubbles of the present invention are adsorbed on the hydrophilic surface through relatively weak, non-covalent interactions. Thus, they are susceptible to being removed, for example by carefully scratching them from the surface. A bulk powder of freeze-dried monodisperse microbubbles, can be obtained.
A fourth object of the present invention concerns freeze-dried monodisperse microbubbles adsorbed on a hydrophilic surface in the form of a single monolayer, such as obtained by the process for preparing freeze-dried microbubbles as previously described.
A fifth object of the present invention concerns freeze-dried monodisperse microbubbles adsorbed on a hydrophilic surface in the form of at least one monolayer, such as obtained by the process for preparing freeze-dried microbubbles as previously described.
A sixth object of the present invention concerns freeze-dried monodisperse microbubbles, in the form of a powder, such as obtained by the process as previously described.
A seventh object of the present invention is a process for preparing an aqueous suspension of monodisperse microbubbles, wherein the process comprises:
According to this object of the present invention, the freeze-dried microbubbles are subjected to an aqueous medium, also referred to as resuspension medium, whereby the microbubbles are detached from the surface.
An aqueous, milky white suspension of microbubbles is initially the result.
The inventors have observed that said suspension of microbubbles gradually, over time, converts into a solution. Indeed, the permeability of the shell leads to diffusion of the gas which is comprised in the core, through the shell, which can lead to the microbubbles to disintegrate and the materials to solubilize, resulting in the obtention of a solution.
This dissolution is not instantaneous, and the aqueous suspension of monodisperse microbubbles according to the present invention is sufficiently stable in air for up to 20 minutes, in particular for up to 10 minutes, more in particular for up to 3 minutes, to be used, for example as a monodisperse contrast agent.
In this respect, the stability also relates to the stability of the monodispersity and the microbubble size, said monodispersity being conserved for up to 20 minutes, After 20 minutes; the microbubbles are susceptible to becoming polydisperse.
Thus, in another embodiment of the invention, the suspension of freeze-dried monodisperse microbubbles, is stable in air for up to 20 minutes, in particular for up to 10 minutes, more in particular for up to 3 minutes, to be used, for example as a monodisperse contrast agent.
Under these conditions less than 10%, in particular less than 1%, of the microbubbles lose their ability to be used as a contrast agent, whereby the change in resonance frequency as compared to the initial resonance frequency measured immediately after the preparation of the suspension is less than 1%, in particular less than 0.1%.
In another embodiment, the present invention concerns a process for preparing an aqueous suspension of microbubbles, as previously defined, wherein said step of resuspending is carried out in a microfluidic chip, in particular in a microfluidic chip comprising pillar based microchannels, or comprising slit microchannels.
This embodiment is, for example, represented by
An eight object of the present invention is a process for preparing an aqueous suspension of monodisperse microbubbles, said process comprising a step of resuspending the freeze-dried monodisperse microbubbles, in the form of a powder, as previously defined, to obtain an aqueous suspension of monodisperse microbubbles,
wherein the microbubbles are physiologically inert,
In this embodiment, the resuspension is not carried out inside a microfluidic chip, but rather is carried out in a vial comprising a bulk powder of microbubbles.
In a preferred embodiment, the present invention concerns a process for preparing an aqueous suspension of monodisperse microbubbles as previously described, wherein the aqueous medium is saturated with a gas, in particular a gas chosen from SF6, air, or perfluorinated hydrocarbons, in particular perfluorohexane, or a mixture of perfluorohexane and SF6, said gas, or mixture of gases, being preferably the same as the gas, or mixture of gases, comprised in, or constituting the core of said microbubbles.
Saturating the aqueous resuspension medium with a gas prevents loss of the gas that is comprised within the core of the microbubbles by diffusion.
In an even more preferred embodiment, the present invention concerns a process for preparing an aqueous suspension of monodisperse microbubbles as previously described, wherein the aqueous medium is phosphate buffered saline, saturated with a gas chosen from air, perfluorinated hydrocarbons or SF6, wherein the gas pressure is below 1000 kPa.
At gas elevated gas pressures, i.e. over 1000 kPa, Ostwald ripening of the microbubbles can occur.
The present invention also relates to a process for preparing an aqueous suspension of monodisperse microbubbles, wherein the process comprises:
The resuspension carried out in a microfluidic chip is depicted in
A ninth object of the present invention relates to an aqueous suspension of monodisperse microbubbles, such as obtained by the process as previously described.
A tenth object of the present invention relates to an aqueous suspension of monodisperse microbubbles, wherein:
In another embodiment, the present invention concerns an aqueous suspension of monodisperse microbubbles as previously defined, wherein the concentration of microbubbles is comprised from 0.1 to 20 w/w % compared to the total weight of the aqueous suspension.
With the expression “0.1 to 20 w/w %” relating to the concentration of microbubbles in the aqueous suspension, should also be understood the following ranges: 0.1 to 15 w/w %, 0.1 to 10 w/w %, 0.1 to 5 w/w %, 1 to 20 w/w %, 5 to 20 w/w %, 10 to 20 w/w %, 15 to 20 w/w %, 1 to 15 w/w %, 5 to 10 w/w %, in particular 8 w/w %.
The freeze-dried monodisperse microbubbles according to the present invention present interesting acoustic properties, due to their high level of monodispersity. These unprecedented acoustic properties can be exploited in several fields.
The present invention also concerns an aqueous suspension of freeze-dried monodisperse microbubbles, such as obtained by the process for preparing an aqueous suspension of monodisperse microbubbles, as previously described, or
an aqueous suspension of monodisperse microbubbles, wherein:
Thus, an eleventh object of the present invention relates to the use of the suspension of freeze-dried monodisperse microbubbles as previously described, or of the freeze-dried monodisperse microbubbles as previously described:
The use of microbubbles for acoustic purposes, such as contrast agent or as ultrasound agents, is subject to several sources of noise that degrades the quality of the image, such as diffusion and speckle.
Clinical ultrasound scanners operate at a narrow frequency bandwidth (typically between 2.5 and 7.5 MHz), and only a small fraction of the microbubbles participates in the generation of the echo. The techniques that would make it possible to improve the signal to noise ratio, or the efficiency quantified by STAR (diffusion to attenuation ratio), by exploiting the harmonic or subharmonic components of the echo, are difficult to implement to commercial microbubbles due to their polydispersity.
Thus, the monodisperse microbubbles according to the present invention present particular advantages in terms of the ability to improve the signal to noise ratio, and their ability to show a well-defined sharp resonance frequency, and are thus of particular interest for use in for acoustic purposes.
The freeze-dried microbubbles of the present invention, after resuspension, have substantially the same acoustic properties as the microbubbles before having been freeze-dried, measured under the same conditions.
In another embodiment, the present invention concerns the use of monodisperse microbubbles as previously described, wherein the microbubbles give an acoustic response at a mechanical index MI lower than 0.4, in response to a driving acoustic pulse.
In another embodiment, the present invention concerns the use of monodisperse microbubbles previously described, wherein the resonance frequency response is comprised from 0.14 MHz to 251.8 MHz, in particular being approximately 1.945 MHz for 5 μm microbubbles having a polydispersity index of 5%.
The resonance frequency response of the microbubbles being inversely proportional to the microbubble size, according to Minnaert's law,
wherein Minnaert's law is defined by Formula 2:
wherein:
In case of heavy gases, having a density higher than the density of air; such as perfluorohydrocarbons, κ=1.1, ρ=1000 kg/m 3 and P0=100 kPa, the above Formula 2 can be rewritten into Formula 3 below:
foRo=3.3μm MHz Formula 3
wherein:
Fo=resonance frequency of the non-coated bubbles
An eleventh object of the present invention is a microfluidic chip comprising:
A typical, non-limiting example of such an arrangement is shown in
The present Invention thus also pertains to a resuspension system, or resuspension device, comprising:
a microfluidic chip as previously defined,
a container filled with gas comprised, or to be comprised in the core of the microbubbles,
tubings to allow provision of a resuspension medium,
optionally, tubings to allow for collecting the resuspended microbubbles from the chip.
The following figures and examples illustrate the implementation of the present invention in some of its embodiments, the figures and examples should not be construed as limiting the scope of the invention.
1 represents the echo obtained with 106 freshly prepared, non-freeze-dried bubbles, 2 represents the echo obtained with 106 resuspended-freeze-dried bubbles, 3 represents the echo obtained in the absence of bubbles, 4 represents the resonance spectrum obtained with 106 fresh, non-freeze-dried bubbles, 5 represents the resonance spectrum obtained with 106 resuspended freeze-dried bubbles, 6 represents the deconvoluted resonance spectrum obtained with 106 fresh, non-freeze-dried bubbles, 7 represents the deconvoluted resonance spectrum obtained with 106 resuspended freeze-dried bubbles, the x-axes correspond to the resonance frequency (Hz) and the y-axes correspond to the mean amplitude (mV).
In
Below, monodisperse PVA-shelled microfluidic microbubbles (PDI<5%) were prepared, encapsulating perfluorocarbon (PFC), or Sulfur hexafluoride (SF6) gas, with polydimethylsiloxane (PDMS)-based microfluidic chips. The problem of long-term storage and transportation, without monodispersity degradation, has been solved by freeze-drying the microbubbles in the form of a monolayer and in the presence of a cryoprotectant.
The polydispersity index is calculated according to Formula 1.
in which
d represents the diameter of the individual microbubbles as measured by optical microscopy.
<d> represents the average of the measured diameter for a population of microbubbles.
The molds for the PDMS chips were fabricated using conventional soft lithography and prepared using replica-molding techniques (J. Cooper McDonald et al., Fabrication of microfluidic systems in poly(dimethylsiloxane), Electrophoresis 2000, 21, p. 27-40). Then, the molds were cut, inlets and outlets were punched through the PDMS, and microfluidic channels sealed with a microscopic glass slide by the application of O2 μlasma with a plasma cleaner (The CUTE, Femto Science Inc., Republic of Korea), which tunes hydrophilicity of the channels as well. Then, plastic tubings were connected to inlet and outlets of the chip.
The microfluidic chip obtained contains two liquid inlets and two corresponding fluid outlets, from which excessive material can be recovered, one gas inlet and one outlet, from which the microbubbles are collected. The outlet includes a collecting tube, aligned along the axis of the collecting channel to avoid coalescence phenomena (e.g., lateral collection), and an entry (e.g., pusher), allowing to increase the flow-rate of the continuous phase, i.e. the liquid phase comprising the shell materials, and thereby tune the bubble concentration, along with their interactions. This step favors the high throughput and reliability of the process. The pusher is helpful, but it is not guaranteed that it is critical. The microfluidic channels consist of the combination of flow-focusing geometry, whose width and height are variable (from 5 μm, as in
The gas-phase of the system, which defines the gas core of the microbubbles, was perfluorohexane (C6F14), or SF6 to enhance the lifetime of the microbubbles as the permeable shell leads to a rapid escape of soluble gases such as air.
Thus, gases that are highly hydrophobic, less soluble, and heavier than air in aqueous solutions were selected in the second-generation microbubbles. The liquid phase was an aqueous solution of polyvinyl alcohol (PVA) (Mw 13,000-23,000, 87-89% hydrolyzed, Sigma-Aldrich) at a concentration of 8 wt. % in 10 mM Phosphate-Buffered Saline (PBS) solution in Milli-Q water.
Due to the slow kinetics of dissolution of the polymer and in order to ensure complete solubilization, PVA was stirred in the aqueous solution at 80° C. overnight before being used as the continuous phase. PVA acts as both a surfactant and cryoprotectant and PVA allows for the formation of a shell around the microbubbles; which is a barrier to reduce gas transport across the bubble interface and thereby increase their lifetimes from several tens of ms to several minutes, a cryoprotectant is added to avoid destruction of the microbubbles during the freeze-drying process (Mensink et al., How sugars protect proteins in the solid state and during drying (review): Mechanisms of stabilization in relation to stress conditions, Eur. J. Pharm. and Biopharm., 114 (2017) 288-295). The external fluid includes both cryoprotectant and surfactants, above CMC and below overlap concentration for the polymer surfactant and the cryoprotectant.
The liquid and gas flows were pressure-driven, pliquid, and pgas, using an MFCS-100 pressure controller system (Fluigent), at pressures from 1.2 to 3.5 bars. These, in turn, taking into account the geometrical features of the microfluidic chip as mentioned in example 1, enable to generate 5 μm diameter microbubbles (PDI <5%) with up to 10 kHz generation frequency with relatively high throughput (˜60×104 microbubbles/min) (
Bubbles generated according to example 3 were transported along with the lateral outlet tubing. Then, the tip of the tube, from which around 104 microbubbles exit the microfluidic chip in a drop of 0.1 which can be characterized as a milky suspension, was moved on an O2 μlasma-treated hydrophilic glass slide (75 mm×25 mm). Thus, the microbubbles were collected in a monolayer manner as individual bubble suspension spots on the slide (
Following the monolayer collection, the microbubbles were pre-frozen for 2 h at −25° C., which is far below the glass transition temperature (Tg) of the used cryoprotectant PVA (˜80° C.). The frozen microbubbles were transferred to a freeze-dryer (FreeZone Labconco, USA) with a shelf temperature of −50° C. for 4 h.
As a result, monodisperse microbubbles, which are attached to the glass slide surface in the form of powder, referred to as freeze-dried cake, was obtained after the freeze-drying process (
The resuspension of 5 μm and 40 μm microbubbles with a PBS solution was performed in a traditional way, which comprises hydration of each spot with an injection of ˜10 μl PBS solution, as shown in
Thus, the freeze-drying of monolayer-collected microbubbles in separate spots enabled the protection of the microbubbles during the process. The thickness of the shell of the dried microbubbles was estimated as 50 nm to 100 nm based on SEM images (
Although the production rate of microfluidic microbubbles does not pose problems thanks to the parallelization, the monolayer constraint, from the collection to the resuspension, requires, in the present stage of the technology, the microbubbles to be placed on surfaces. Therefore, the packaging and thus, the resuspension of monodisperse freeze-dried microbubbles are different from that of traditional microbubbles. A typical glass-PDMS microfluidic chip which enables packaging and resuspension of around 106 freeze-dried microbubbles that are present in the form of a monolayer on the glass slide was developed (
The qualitative echogenicity of the freeze-dried PVA microbubbles with 5 μm in diameter was tested using an Aixplorer ultrasound system (V12). The probe used was the XC6-1 (192 transducers, piezo patch: 0.33 mm, probe radius: 60 mm). A sinusoidal burst centered on 3.21 MHz (bandwidth of 0.5 to 5 MHz) with a PRF=1000 Hz was sent. The freeze-dried microbubbles were transported to an institute located in Paris that has excellent expertise on acoustic imaging, LANGEVIN, then resuspended in a PBS solution, and ultrasound imaging experiments were carried out. A typical image is shown in
The stationary backscattered acoustic measurements of 5 μm PVA microbubbles were performed in a pillar-based microfluidic resuspension. Unlike the resuspension system, the PDMS microchannels were bonded to another blank-flat PDMS in order to avoid glass's strong acoustic reflectivity the acoustic impedance. The bubbles were generated as mentioned in example 3, but the outlet tubing (i.e. transfer tubing) was inserted to the inlet of the resuspension system. Then, the generated bubbles homogeneously distributed inside the chip and flowed until the outlet of the system.
When the bubbles started to come out from the chip, out of the outlet of the resuspension system, the chip was disconnected from the generation chip and the acoustic measurements were performed. A typical of 105-106 bubbles was used for the measurements. For the reference measurement, the chip was filled with the deionized water and the acoustic measurement was performed.
A focused ultrasound transducer with a 38 mm focal length and a central frequency of 2.25 MHz was used. The transducer was connected to an arbitrary wavefunction generator and a PicoScope 5242D for data acquisition. The transducer was used as an emitter and a receiver. Sinusoidal 1-cycle burst mode 5V signal is generated and used to excite bubbles. The used focus acoustic transducer was coupled with a 3D printed waveguide, which was fully filled with an acoustic gel that enabled propagation of a generated acoustic wave through the transducer to the first PDMS layer. Then, the wave travels along with the chip, as shown in
The echo from the same bubble population was measured several times for 20 minutes. Each measurement consisted of 1000 measurements (1000 measurements take approximately 45 seconds) and each echo processed to FFT spectrum, then were averaged. Finally, the resulted resonance curves were Gaussian-fitted. The first three minutes (measurements A, B, C), we obtained 0.1% stability on the resonance frequency of the bubbles.
As shown in
In conclusion, this result showed that our monodisperse bubbles are characterized with a narrow-band (around 15%) resonance response with high stability (0.1%), which enables to track the resonance frequency change, due to ambient pressure change, with 0.1% (leading to sub-kPa pressure sensitivity), which is 10-fold better than the clinically required sensitivity (±2 kPa). Microbubbles available up to now suffer from achieving this sensitivity and performing reproducible measurements due to their broadband resonance response originated from their polydispersity nature.
A monolayer of freeze-dried microbubbles on a glass slide was prepared according to example 4. The microbubbles were stored in a refrigerator for 18 months, before being resuspended according to the procedure of example 6.
The resulting powder showed a CV below 6% (
A glass-PDMS container of which enables packaging and resuspension of ˜106 freeze-dried bubbles that are present in the form of a monolayer on a glass slide was developed (see
The dimension of the resuspension system was 20 mm×75 mm×0.5 mm that lead to a concentration of 106 bubbles/mL
The container was then placed in a sealed vial which was filled with PFC or SF6 gases to resuspend the bubbles with the desired gas core. When the bubbles were completely hydrated, which took a few seconds (
The echogenicity of microbubbles was determined in a similar way as for example 7.
The experiment was carried out with Aixplorer ultrasound system (V12). The probe used was the XC6-1 (192 transducers, piezoPitch: 0.33 mm, probe radius: 60 mm). A sinusoidal burst centred on 3.21 MHz (bandwidth of 0.5 to 5 MHz) with a PRF=1000 Hz was sent.
The echogenicity of the freeze-dried bubbles was determined both in the B-mode and in the CEUS mode, which is the most commonly used mode in clinics to distinguish better the bubbles from the surrounding.
The resulting ultrasound images are shown in
The Acoustic properties of microbubbles were analyzed for bubbles before freeze-drying and bubbles that were resuspended after having been freeze-dried.
The acoustic characterization setup, instrumentation, example of typically emitted signals, received echoes, and resonance spectra for the backscattered acoustic measurements of stationary microbubbles that were used in this experiment are shown in
A small PDMS-based structure as a measurement chamber (35 mm×10 mm×1 mm) was used. The thickness of the walls of the PDMS container is 10 mm, more than ten times larger than the initial wavelength. This ensures propagation of the initial wave deep in the system and produces echoes from the container walls. The structure was replicated with PDMS from a mold. A function generator (Tektronix AFG 2021) was used to generate a Sinusoidal 1-cycle burst signal with a 1-ms pulse repetition period (see
The peak negative acoustic pressure, as measured by a hydrophone, was fixed to 134 kPa. A PicoScope (5242D) was used for data acquisition, and its dedicated software was used to monitor and record the detected signal. It acquired 1 waveform/45 ms and one waveform (i.e., echo) consisted of 3125 data points.
Typically, each measurement took 45 s, yielding 1000 waveforms. Each echo was taken from the focal point, as the region of interest. Its Fourier transform is then calculated (via an HT algorithm) and averaged with a MATLAB program.
The obtained resonance spectra are shown in
Then, this spectrum was deconvoluted from the spectra obtained with the bubbles (
These results show that the freeze-drying process does not have an effect on the acoustic properties of the microbubbles as they show an indistinguishable acoustic response.
| Number | Date | Country | Kind |
|---|---|---|---|
| 20201537.6 | Oct 2020 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2021/077785 | 10/7/2021 | WO |
