Patent Application
20220113232
The present disclosure relates to distribution of particles, dispensing of fluid containing particles, and manufacture of a product containing particles.
A dispensing operation of ejecting a uniform amount of solution is carried out in, for example, a sampling operation for component analysis, or a vial filling process for filling an industrial product into vials, wherein the principal component of the product is a small amount of solution. The development of an automatic analyzer that automatically performs a dispensing operation has been also developed (Patent Documents 1 and 2).
In a case of a liquid in which substances having largely different densities are mixed, dispersed, or dissolved, such as a mixture of a plurality of types of solutions, or a solution containing microparticles, it is necessary to keep the concentrations of the substances in the liquid to be dispensed constant before the dispensing and after the start of the dispensing (during the dispensing process), in order to dispense the liquid so that the concentrations of the substances are uniform. To solve this problem, a physical stirring operation using magnetic microparticles or ultrasonic waves in a storage part has been proposed (Patent Documents 3 and 4).
In the above-described dispensing method with physical stirring, however, it is necessary to optimize the stirring method and parameters of respective operations according to components of samples and the scale.
Besides, in a case of a sample containing a living component such as cells, there are concerns that the activity thereof might deteriorate due to physical stimulation of stirring.
In light of this, the present disclosure, in one aspect, provides a novel distribution method with which particle components such as cells can be dispensed.
In one aspect, the present disclosure relates to a method for distributing particles, the method including:
dispersing the particles in a plastic fluid; and
dispensing the plastic fluid containing the particles.
In one aspect, the present disclosure relates to a producing method for producing a product that includes a particle and a container for the particle, the producing method including:
dispensing a plastic fluid in which the particles are dispersed, from a storage part in which the plastic fluid is stored, to a plurality of the containers.
Further, in another aspect, the present disclosure relates to a composition to be used in dispensing in the distribution method or the producing method according to the present disclosure, the composition containing a substance for converting a liquid in which particles are dispersed, or a liquid that disperses particles, into a plastic fluid.
Still further, in another aspect, the present disclosure relates to a composition containing a cell cryopreservation solution and a substance for converting the cell cryopreservation solution into a plastic fluid.
According to the present disclosure, in one aspect, distribution in which unevenness of the amount (or density) of particles is suppressible without stirring in a storage part during a distributing operation can be provided.
The present disclosure is based on the following findings: in a case where particles such as cells or beads are dispensed, the use of a plastic fluid can suppress fluctuations in the concentration or density of particles in an aliquot dispensed, even without a stirring operation during the dispensing process.
The present disclosure is also based on the following findings: when dispensing without use of a stirring operation during a dispensing process is made possible, even a living particle component such as cells, or a fragile particle component can avoid damage caused by stirring, while fluctuations in the concentration or density of the particles in an aliquot dispensed can be suppressed.
The present disclosure is further based on the following findings: when dispensing without use of a stirring operation during a dispensing process is made possible, gas contamination (mixing of gas (air bubble) into the liquid) in a storage part (reservoir) can be suppressed, whereby fluctuations in the dispensed amount can be suppressed.
The present disclosure is still further based on the following findings: using a plastic fluid when a solution is dispensed with use of a pump and a tube makes it possible to feed the solution in laminar flow in the tube, thereby making it easier to maintain the same concentration of particles as the concentration during sucking. In addition, the present disclosure is based on the following findings: when feeding the solution in laminar flow is made possible, collapse of interface between the solution and a gas phase is suppressed, which makes it unlikely that the solution would contain gas.
The present disclosure, however, is not limited by these findings.
[Distribution Method, Dispensing Method]
In one aspect, the present disclosure relates to a method for distributing particles, the method including dispersing the particles in a plastic fluid, and dispensing the plastic fluid containing the particles.
In the distribution method according to the present disclosure, for example in a case where the particles are cells, an exemplary plastic fluid is a plastic fluid obtained by mixing a specific compound described below in a medium or a cryopreservation solution.
The distribution method for distributing particles according to the present disclosure, therefore, can be paraphrased as follows. Specifically, in one aspect, the present disclosure relates to a dispensing method that includes making a liquid for a particle-containing liquid into a plastic fluid, and aliquoting the particle-containing plastic fluid.
With the distribution method and the dispensing method of the present disclosure, in one or a plurality of embodiments, a particle-containing liquid (plastic fluid) can be distributed or dispensed uniformly in density and uniformly in amount, without an operation such as a stirring operation. In one or a plurality of embodiments, therefore, the distribution method and the dispensing method of the present disclosure include distributing or dispensing a particle-containing plastic fluid in aliquots.
The following description describes particles and plastic fluids.
[Particles]
In the distribution/dispensing method of the present disclosure, “particles” refer to those that can be dispensed when mixed in a liquid.
The particles may be in a solid or liquid form.
The particles in one or a plurality of embodiments are cells, microorganisms, liposomes, medicine-containing particles, cosmetic components such as pigments, beads, or colloidal particles.
Since a stirring operation during a distribution/dispensing process is not essential in the distribution/dispensing method of the present disclosure, the method is preferable for distributing/dispensing particles sensitive to shear stress (physical stress). The particles are not necessarily limited to these.
The “cells” can encompass cells derived from animals, and cells derived from plants. The cells in one or a plurality of embodiments are cultured cells. Exemplary cultured cells are stem cells; the stem cells are, for example, pluripotent stem cells such as embryonic stem cells (ES cells) and induced pluripotent stem cells (iPS cells), or multipotential stem cells such as mesenchymal stem cells, hematopoietic stem cells, and tissue stem cells.
Examples of beads include polymer beads, ceramic beads, metal beads, and metal oxide beads. Examples of the bead form include magnetic beads, bead carriers, and abrasive grains.
Examples of colloid include emulsion and suspension.
In the present disclosure, the “distribution of particles” encompasses dispensing of a mixture of particles and a liquid.
In the present disclosure, the “liquid” can mean both of a liquid that is not a plastic fluid, and a plastic fluid. Unless specified otherwise, the “liquid” means a liquid that is not a plastic fluid.
[Plastic Fluid]
In the present disclosure, the “plastic fluid” refers to a fluid that requires a yield stress to be made to flow, that is, a fluid having a yield value. The plastic fluid may be a Bingham fluid, or a non-Bingham fluid. In the present disclosure, the “plastic fluid” refers to a plastic fluid that can suppress the sedimentation of particles to be distributed (dispensed), or preferably can hold particles without sedimentation in a standstill state.
In the present disclosure, in one or a plurality of non-limiting embodiments, the plastic fluid can be obtained by mixing a liquid that is not a plastic fluid and a specific compound.
The specific compound is a compound that can convert a liquid that is not a plastic fluid into a plastic fluid, and in one or a plurality of non-limiting embodiments, compounds disclosed in WO2014/017513 or compounds described below can be used as the specific compound.
The specific compound for converting a liquid that is not a plastic fluid into a plastic fluid is not particularly limited, but it is, for example, a high molecular compound, or preferably a high molecular compound having an anionic functional group.
Examples of the anionic functional group include carboxy group, sulfo group, phosphate group, and salts of these; among these, carboxy group or a salt thereof is preferred.
As the high molecular compound, a high molecular compound having one, two, or more selected from the group consisting of the anionic functional groups can be used.
Preferable specific examples of the specific compound for converting a liquid that is not a plastic fluid into a plastic fluid include, though not particularly limited to these, a polysaccharide in which ten or more monosaccharides (e.g., triose, tetrose, pentose, hexose, or heptose) are polymerized; more preferably, the specific compound is an acidic polysaccharide having an anionic functional group. The “acidic polysaccharide” referred to herein is not particularly limited as long as it has an anionic functional group in its structure. The acidic polysaccharide is, for example, a polysaccharide having an uronic acid (e.g., glucuronic acid, iduronic acid, galacturonic acid, or mannuronic acid), a polysaccharide having a sulfate group or a phosphate group in a part of its structure, or a polysaccharide having both of the structures. The acidic polysaccharide encompasses, not only polysaccharides obtained from nature, but also polysaccharides produced by microorganisms, polysaccharides produced by genetic engineering, and polysaccharides artificially synthesized with use of an enzyme. More specifically, the acidic polysaccharide is, for example, constituted of one, two, or more selected from the group consisting of hyaluronic acid, gellan gum, deacylated gellan gum (hereinafter referred to as DAG in some cases), rhamsan gum, diutan gum, xanthan gum, carrageenan, xanthan gum, hexuronic acid, fucoidan, pectin, pectic acid, pectinic acid, heparan sulfate, heparin, heparitin sulfate, keratosulfate, chondroitin sulfate, dermatan sulfate, rhamnan sulfate, and salts of these. The polysaccharide is preferably hyaluronic acid, DAG, diutan gum, xanthan gum, carrageenan, or a salt of any of these; more preferably the polysaccharide is DAG, considering that when DAG is used at a low concentration, particles are suspended, and are easily collected. Examples of the salt referred to herein include: salts of alkali metals such as lithium, sodium, and potassium; salts of alkali earth metals such as calcium, barium, and magnesium; and salts of aluminum, zinc, steel, iron, ammonium, organic bases, and amino acids.
These high molecular compounds (polysaccharides) preferably have a weight-average molecular weight of 10,000 to 50,000,000, more preferably, 100,000 to 20,000,000, and further preferably 1,000,000 to 10,000,000. For example, the molecular weight can be measured in terms of pullulan by gel permeation chromatography (GPC). Alternatively, as DAG, phosphorylated DAG can be used. The phosphorylation can be performed by a known method.
In one or a plurality of embodiments, as the polysaccharide, a plurality (preferably two) of the polysaccharides can be used in combination. The type of the combination of polysaccharides is not limited particularly; preferably, the combination includes at least DAG or a salt thereof. More specifically, the preferable combination of polysaccharides includes DAG or a salt thereof, and a polysaccharide other than DAG or a salt thereof (e.g., xanthan gum, alginic acid, carrageenan, diutan gum, methylcellulose, locust bean gum, or a salt of any of these). Examples of a specific combination of polysaccharides include: DAG and rhamsan gum; DAG and diutan gum; DAG and xanthan gum; DAG and carrageenan; DAG and xanthan gum; DAG and locust bean gum; DAG and K-carrageenan; DAG and sodium alginate; and DAG and methylcellulose, though not limited to these.
Further preferable specific examples of the specific compound include hyaluronic acid, deacylated gellan gum, diutan gum, carrageenan, xanthan gum, and salts of these, among which deacylated gellan gum and salts of the same are more preferable. In the present disclosure, deacylated gellan gum is a linear high molecular weight polysaccharide containing four molecules of saccharides as constituent units, the saccharides being 1,3-bonded glucose, 1,4-bonded glucuronic acid, 1,4-bonded glucose, and 1,4-bonded rhamnose; the polysaccharide is expressed by Formula (I) below, where R1 and R2 each represent a hydrogen atom, and n represents an integer of 2 or more. Here, R1 may include a glyceryl group, and R2 may include an acetyl group; the content of the glyceryl group and the acetyl group is preferably 10% or less, or more preferably 1% or less.
The mechanism of converting the liquid into a plastic fluid varies with the above-described specific compounds; in the case of deacylated gellan gum, when mixed with a liquid, the deacylated gellan gum takes in metal ions (for example, calcium ions) in the liquid, and forms a structure in an undefined shape with the metal ions being interposed therein, to suspend the particles. In one or a plurality of embodiments, a liquid as a plastic fluid prepared with use of deacylated gellan gum has a viscosity of 8 mPa·s or less, preferably 4 mPa·s or less, and more preferably 2 mPa·s or less considering the collectability of the particles. The viscosity of the liquid as a plastic fluid, however, is not limited particularly, and may exceed the above-described values.
The specific compound to convert the liquid into a plastic fluid can be obtained by chemical synthesis, but in a case where the compound is a natural product, the compound is preferably obtained by extraction and separation/purification with a conventional technique from any of various plants, animals, and microorganisms containing the compound. In the extraction, water or a supercritical gas may be used so that the compound can be extracted efficiently. For example, in the gellan gum producing method, the following may be carried out: microorganisms producing gellan gum are cultured in a fermentation medium, then, a mucous substance produced extracellularly is collected by a common purification method, and dried, crushed, etc., followed by pulverization. In a case of deacylated gellan gum, the following may be carried out: a mucous substance is subjected to an alkali treatment when being collected, and the glyceryl and acetyl groups bound to 1,3-bonded glucose residues are collected after being acylated. Regarding the purification method, for example, any of the following may be used alone, or in combination in an arbitrary order, and repeatedly, so as to remove impurities for purification: liquid-liquid extraction; fractional precipitation; crystallization; various types of ion-exchange chromatography; gel filtration chromatography using sephadex LH-20 or the like; adsorption/desorption of an active substance by adsorption chromatography using activated charcoal, silica gel, etc., or thin-layer chromatography; and high-performance liquid chromatography using a reversed-phase column. Examples of gellan gum producing microorganisms include Sphingomonas elodea, and microorganisms obtained by modifying genes of Sphingomonas elodea, though not limited to these.
In the case of deacylated gellan gum, a commercially available product may be used, which is, for example, “KELCOGEL (registered trademark of C. P. Kelco) CG-LA” manufactured by Sanshin Co., Ltd., or “KELCOGEL (registered trademark of C. P. Kelco)” manufactured by San-Ei Gen FFI Co., Ltd. Alternatively, “KELCOGEL (registered trademark of C. P. Kelco) HT” manufactured by San-Ei Gen FFI Co., Ltd. can be used as native gellan gum.
[Concentration of Specific Compound in Plastic Fluid]
The concentration of the specific compound in the plastic fluid (mass/volume %, hereinafter simply referred to as “%”) is dependent on the type of the specific compound, and can be set appropriately in such a range that the plastic fluid can hold cells in a storage bottle without sedimentation in a standstill state; the concentration of the same is normally 0.0005% to 1.0%, preferably 0.001% to 0.4%, more preferably 0.005% to 0.1%, and further preferably 0.005% to 0.05%. For example, in a case of deacylated gellan gum, the concentration of the same is 0.001% to 1.0%, preferably 0.003% to 0.5%, more preferably 0.005% to 0.1%, further preferably 0.01% to 0.05%, and still further preferably 0.02% to 0.05%. For example, in a case of xanthan gum, the concentration of the same is 0.001% to 5.0%, preferably 0.01% to 1.0%, more preferably 0.05% to 0.6%, and further more preferably 0.3% to 0.6%. For example, in a case of mixture of K-carrageenan and locust bean gum, the concentration of the same is 0.001% to 5.0%, preferably 0.005% to 1.0%, more preferably 0.01% to 0.1%, and most preferably 0.03% to 0.05%. In a case of native gellan gum, the concentration of the same is 0.05% to 1.0%, and more preferably 0.05% to 0.1%.
In a case where a plurality of types (preferably two types) of the above-described polysaccharides are used in combination, the concentration of the polysaccharides can be set appropriately in such a range that the plastic fluid can hold cells in the liquid without sedimentation in a standstill state. For example, in a case where a combination of DAG or a salt thereof, and a polysaccharide other than DAG or the salt thereof, is used, an exemplary concentration of DAG or the salt thereof is 0.005 to 0.02%, and preferably 0.01 to 0.02%; and an exemplary concentration of the polysaccharide other than DAG or the salt thereof is 0.005 to 0.4%, and preferably 0.1 to 0.4%. Examples of the combination of specific concentration ranges include the following.
DAG or salt thereof: 0.005 to 0.02% (preferably 0.01 to 0.02%)
Polysaccharide other than DAG
xanthan gum: 0.1 to 0.4%
sodium alginate: 0.1 to 0.4%
locust bean gum: 0.1 to 0.4%
methylcellulose: 0.1 to 0.4% (preferably 0.2 to 0.4%)
carrageenan: 0.05 to 0.1%
diutan gum: 0.05 to 0.1%
The concentration can be calculated by the following formula.
Concentration (%)=mass of specific compound (g)/volume of liquid (ml)×100
The specific compound can be converted to still another derivative by chemical synthesis, and the derivative thus obtained can be also used effectively in such a cell culturing method according to the present disclosure. Specifically, in a case of deacylated gellan gum, a derivative obtained by substituting the hydroxyl group corresponding to R1 and/or R2 of the compound expressed by Formula (I) with the following can also be used in the present invention: a C1-3 alkoxy group; a C1-3 alkylsulfonyl group; a residue of a monosaccharide such as glucose or fructose; a residue of an oligosaccharide such as sucrose or lactose; a residue of an amino acid such as glycine or arginine; etc. It is also possible to crosslink the compound by using a cross-linker such as 1-ethyl-3-(3-di-methylaminopropyl)carbodiimide (EDC).
The specific compound or a salt thereof may exist as an arbitrary crystal form depending on production conditions, and may exist as an arbitrary hydrate. These crystal forms, hydrates, and mixtures thereof are also encompassed in the present invention. The specific compound may also exist as a solvate containing an organic solvent, such as acetone, ethanol, or tetrahydrofuran; all of these forms are encompassed in the present disclosure.
The specific compound may exist in a form of a tautomer or a geometric isomer generated by endocyclic or exocyclic isomerization, or a mixture of tautomers or geometric isomers, or alternatively, a mixture of any of these. In the present disclosure, the specific compound when having an asymmetric center may exist in a form of a resolved optical isomer or a mixture containing them at an arbitrary ratio, irrespective of whether the specific compound is generated by isomerization or not.
In one or a plurality of embodiments, the liquid as a plastic fluid can be produced by adding a solution or a dispersion of the specific compound to a liquid culture medium. As the specific compound aggregates with ions (the compound assembles via ions), or the specific compound forms a three-dimensional network, a metal ion is preferably added as required. In one or a plurality of embodiments, the metal ion is a divalent metal ion. In one or a plurality of embodiments, examples of the divalent metal ion include calcium ion, magnesium ion, zinc ion, ferrous ion, and copper ion. In one or a plurality of embodiments, the concentration of the metal ion is 0.1 mM to 300 mM, 0.5 mM to 100 mM, or 0.5 mM to 10 mM.
[Yield Value of Plastic Fluid]
In the present disclosure, the yield value of the plastic fluid used in the present disclosure is preferably at such a level that the plastic fluid can hold particles without sedimentation in a standstill state. With a view to holding particles, the plastic fluid used in the present disclosure preferably has a yield value of 0.02 Pa or more, and more preferably, 0.03 Pa or more. The plastic fluid used in the present disclosure has a yield value of, for example, 0.2 Pa or less, or 0.1 Pa or less.
[Automated Pipetting System]
The distribution/dispensing method of the present disclosure can be favorably applied to dispensing by an automated pipetting system. With the distribution/dispensing method of the present disclosure, in one or a plurality of non-limiting embodiments, it is possible to suppress at least one of the unevenness of the dispensed amount for an aliquot, the unevenness of the particle density, and the unevenness of the cell viability in a case where the particles are cells, when the dispensing is performed by the automated pipetting system.
The automated pipetting system is not particularly limited in the present disclosure, and examples of the same include: a type that performs sucking from a storage part (reservoir) with use of a pump unit including a feeding pipe and a pump, and performs ejecting to vials or a multiwell plate; and a type that performs dispensing from a storage part to a multiwell plate with use of a dispensing pipet head that is capable of sucking and ejecting.
In one or a plurality of embodiments, the automated pipetting system of the present disclosure includes a control unit for controlling a pump unit, a dispensing pipet head, and the like. In one or a plurality of embodiments, the control unit controls a pump unit, a dispensing pipet head, and the like, so as to dispense a particles-dispersed plastic fluid stored in a storage part in aliquots into a plurality of containers.
[Producing Method]
In another aspect, the present disclosure relates to a producing method for producing a product including a particle and a container for the particle, the producing method including dispensing a plastic fluid in which the particles are dispersed, from a storage part in which the plastic fluid is stored, to a plurality of the containers.
The producing method of the present disclosure can be described differently as follows. In another aspect, the present disclosure relates to a producing method for producing a product that includes a liquid and a container for the liquid, the producing method including dispensing the liquid from a storage part of the liquid into a plurality of the containers, wherein the liquid is a plastic fluid containing particles.
With the producing method of the present disclosure, in one or a plurality of embodiments, it is possible to produce products having substantially uniform amounts (or concentrations) of particles and/or substantially uniform amounts of liquid. With the producing method of the present disclosure, in one or a plurality of embodiments, it is possible to dispense substantially the same amount (or concentration) of particles and/or the same amount of liquid as that dispensed into a container at the start of dispensing, even when a remaining amount of the plastic fluid or liquid in a storage part arranged in an automated pipetting system becomes 20% or less, 15% or less, 10% or less, 5% or less, 4% or less, 3% or less, 2% or less, or 1% or less of the amount before the start of dispensing. Besides, in a case where the remaining amount of the plastic fluid or liquid in the storage part arranged in the automated pipetting system becomes equal to or less than the dispensing amount, all of the remainder can be dispensed in one container.
In one or a plurality of embodiments, the producing method of the present disclosure includes dispensing a particle-dispersed plastic fluid in aliquots into a plurality of containers. In one or a plurality of particularly non-limiting embodiments, the producing method of the present disclosure includes dispensing the particle-dispersed plastic fluid or liquid stored in a storage part arranged in an automated pipetting system, in aliquots into a plurality of containers. In one or a plurality of embodiments, the producing method of the present disclosure includes producing a plurality of the products dispensed in aliquots, by using an automated pipetting system.
In the present disclosure, “dispensing in aliquots” encompasses dispensing particles/liquid into a plurality of containers in such a manner than the containers contain substantially uniform amounts (or concentration) of the particles and/or substantially uniform amounts of the liquid. In the present disclosure, “substantially uniform amounts (or concentration) of the particles” means that a relative error of an amount (or concentration) (Yp) of particles dispensed in a container with respect to a desired amount (or concentration) (Xp) of the particles ({(Xp−Yp)/Xp}×100) is ±15% or less, ±14% or less, ±13% or less, ±12% or less, ±11% or less, ±10% or less, ±9% or less, ±8% or less, ±7% or less, ±6% or less, ±5% or less, ±4% or less, ±3% or less, ±2% or less, ±1% or less, or ±0.55% or less. In the present disclosure, “substantially uniform amounts of the liquid” means that a relative error of an amount (Yl) of liquid dispensed in a container with respect to a desired amount (Xl) of the liquid ({Xl−Yl)/Xl}×100) is ±10% or less, ±9% or less, ±8% or less, ±7% or less, ±6% or less, ±5% or less, ±4% or less, ±3% or less, ±2% or less, ±1% or less, or ±0.55% or less.
The “plurality of containers (or products)” in the present disclosure are 50 or more, 60 or more, 70 or more, 80 or more, 90 or more, or 100 or more in number, though the number is not particularly limited to these.
The product that can be produced by the producing method of the present disclosure is, for example, vial products in which cultured cells, liposomes, or medicine-containing particles are dispensed; other examples of the same include cosmetics, and pharmaceutical products.
[Composition]
Further, in another aspect, the present disclosure relates to a composition to be used in the dispensing in the distribution method or the producing method according to the present disclosure, the composition containing a substance for converting a liquid in which particles are dispersed, or a liquid that disperses particles, into a plastic fluid.
The composition according to the present disclosure may be in a solid or powdered state, or in a liquid state.
As the above-described “substance for converting . . . into a plastic fluid”, the above-described specific compound can be used.
The composition according to the present disclosure may further contain another component, that is, a component other than the above-described substance (specific compound).
Examples of the above-described other component include a cell culturing medium component, and a component of a cell cryopreservation solution, in a case where the particles are cells. The cell culturing medium component can be appropriately selected according to the cells. In the present disclosure, the cell cryopreservation solution may be a medium for cell cryopreservation. Exemplary components of the cryopreservation solution include a cell cryoprotectant agent, an intracellular cryoprotectant agent, and an extracellular cryoprotectant agent.
In another aspect, therefore, the present disclosure relates to a composition containing a cell cryopreservation solution, and a substance for converting the cell cryopreservation solution into a plastic fluid. The composition according to the present disclosure, in one or a plurality of embodiments, is a cell cryopreservation solution in which a “substance for converting the cell cryopreservation solution into a plastic fluid” is dissolved, whereby the cell cryopreservation solution is converted into a plastic fluid. Another composition according to the present disclosure, in one or a plurality of embodiments, is a combination of a cell cryopreservation solution and a “substance for converting the cell cryopreservation solution into a plastic fluid” held in such a form that they are not mixed with each other.
In a case where the above-described other component is a component of a cell cryopreservation solution, a metal ion is preferably added as required, as the specific compound aggregates with the metal ions, or the specific compound forms a three-dimensional network. In one or a plurality of embodiments, the metal ion is a divalent metal ion. In one or a plurality of embodiments, examples of the divalent metal ion include calcium ion, magnesium ion, zinc ion, ferrous ion, and copper ion. In one or a plurality of embodiments, the concentration of the metal ion is 0.1 mM to 300 mM, 0.5 mM to 100 mM, or 0.5 mM to 10 mM.
The present disclosure also relates to one or a plurality of non-limiting embodiments described below:
[1] A method for distributing particles, the method including:
dispersing the particles in a plastic fluid; and
dispensing the plastic fluid containing the particles.
[2] The method according to Item [1], wherein the dispensing is carried out by an automated pipetting system.
[3] The method according to Item [1] or [2], wherein the particles are cells.
[4] A method for producing a product that includes a particle and a container for the particle, the producing method including:
sucking an aliquot of plastic fluid in which the particles are dispersed from a storage part in which the plastic fluid is stored, discharging it into the container, and repeating these processes for a plurality of the containers.
[5] The method according to Item [4], wherein the dispensing is carried out by an automated pipetting system.
[6] The method according to Item [4] or [5], wherein the particles are cells.
[7] A composition to be used in the dispensing in the distribution method according to any one of Items [1] to [3], or the producing method according to any one of Items [4] to [6], the composition containing a substance for converting a liquid in which particles are dispersed, or a liquid that disperses particles, into a plastic fluid.
[8] A composition containing a cell cryopreservation solution, and a substance for converting the cell cryopreservation solution into a plastic fluid.
Hereinafter, although the following description describes the present disclosure in more detail by way of examples, these are illustrative, and the present disclosure is not limited to these examples.
An automated pipetting device (
[Assessment Model]
Formula (I) shown below was used as a model for assessing the quality of vial products of cultured cells by dispensing using an automated pipetting device. Formula (I) below is intended to determine an index Y of the number of effective cells in one vial bottle (see
Y=(V/Vt)ts,Fs·(D/D0)ts,Fs·(P/P0) (I)
Parameters in Formula (I) are ts and Fs. “ts” represents a period from the start of dispensing to the suction from the liquid reservoir bottle in the storage part (hereinafter, this period is referred to as “suspension time”) (h). “Fs” represents a frequency of shaking (s−1) of the liquid reservoir bottle.
“(V/Vt)ts,Fs” is a relative value of the dispensed amount. “Vt” represents a set dispensing amount, and “V” represents a dispensed aliquot amount.
“(D/D0)ts,Fs” is a relative value of the density. “Do” represents the density (the number of particles (or the number of cells)/ml) of an aliquot at the dispensing start time (ts=0, dispersed state), and “D” represents the density of dispensed aliquot.
“(P/P0)” is a cell viability, which is calculated by the following formula.
(P/P0)=αts,Fs×βts,Fs×γts,Fs
γts,Fs=n1/n0
βts,Fs=n2/n1
αts,Fs=n3/n2
n0: initial viable cell count
n1: viable cell count after dispensing
n2: viable cell count after freezing and rewarming (thawing)
n3: adherent cell count at 24 hours after seeding
γ represents a survival ratio determined based on a cell count before stirring and a cell count after stirring.
β represents a survival ratio determined based on a cell count before freezing and a cell count after rewarming (thawing).
α represents an adherent cell ratio determined based on an adherent cell count before seeding and an adherent cell count at 24 hours after seeding.
Beads and a cryopreservation solution (trade name: STEM-CELLBANKER® GMP grade, produced by ZENOAQ) were placed in a liquid reservoir bottle, so that 100 ml of a bead suspension solution having a bead density of 1.0×106 beads/ml was produced. By using an autopipetter and a 50-ml pipet, pipetting inside the bottle was carried out 10 times at a high speed, so as to make the concentration uniform. The bottle having a uniform concentration was set in a storage part in the automated pipetting device shown in
As illustrated in
(D/Do) was calculated as to each of 100 vials into which suspension solutions stirred at frequencies of shaking of Fs=0, 0.9, and 1.6 s−1 were dispensed. The results are shown in
As illustrated in
With an automated pipetting device that was made capable of pump-sucking while shaking a liquid reservoir bottle, 100 ml of a cryopreservation solution (trade name: STEM-CELLBANKER® GMP grade, produced by ZENOAQ) was dispensed to 102 vials over about 30 minutes. The sucking from the liquid reservoir bottle was carried out with a tip of a feeding pipe being fixed at a position of 5 mm above the bottom surface of the bottle.
As to each of 102 vials to which the solution was dispensed, the dispensed amount was measured. The results are shown in
As shown in
Thus, a possibility was indicated that with too great a frequency of shaking (Fs=5.8 s−1), bubbles are sucked into the feeding pipe, which causes the dispensed amount to decrease in the latter half of an operation.
Test Examples 1 and 2 proved that in a case of a common liquid such as a liquid preservation solution, stirring at a speed at a certain level or more is required so as to make the concentration of particles such as beads or cells uniform among vials; however, it is necessary that the stirring is not too fast so that the amount to be dispensed in a vial is made uniform among the vials.
Next, dispensing was carried out in the same manner as that described above except that the cryopreservation solution to which the compound A (deacylated gellan gum, produced by Nissan Chemical Corporation) was added (the concentration of the compound A: 0.06%) was placed in a liquid reservoir bottle, and shaking was not carried out (Fs=0). Then, the dispensed amount was measured. The results are shown in
As illustrated in
In place of the beads of Test Examples 1 and 2, hiPS cells cultured in a T-225 flask (D2 strain, StemFit medium) were used (see
Influences of the time of shaking applied during a predetermined suspension time (1 h or 4 h) on the viability (P/P0) were confirmed. The results are shown in
“ts” in the present test example represents a time since the cell suspension solution was prepared with use of a cryopreservation solution until the solution was frozen. In
As illustrated in
[Production of Plastic Fluid]
Calcium chloride was added to a cryopreservation solution (trade name: STEM-CELLBANKER® GMP grade, produced by ZENOAQ) so that the concentration of calcium chloride was 2 mM, and 92.5 ml of the solution was placed in a liquid reservoir bottle. Using a syringe and an injection needle, 7.5 ml of a compound A (deacylated gellan gum, produced by Nissan Chemical Corporation) was added so that the concentration thereof was 0.06%, was mixed by inversion, and was stored overnight in a refrigerator.
Beads and a compound-A-added cryopreservation solution were placed in a liquid reservoir bottle, so that 100 ml of a bead suspension solution having a bead density of 1.0×106 beads/ml, was produced. By using an autopipetter and a 50-ml pipet, pipetting inside the bottle was carried out 10 times at a high speed, so as to make the concentration of the beads in the bottle uniform. The bottle having a uniform concentration of the beads was set in a storage part in the above-described automated pipetting device, the tip of a feeding pipe was inserted into the bottle, and the position of the tip of the feeding pipe was adjusted to a position of 5 mm under the surface of the suspension solution. Thereafter, the suspension solution was dispensed to 100 freezing vials by the automated pipetting device so that each vial contained 1 ml. The bead density in each vial to which the suspension solution was thus dispensed was measured by using an auto cell counter. See
Bead densities (D/D0) were calculated as to the following: vials to which the suspension solution obtained by adding the compound A to the cryopreservation solution was dispensed; and vials to which the suspension obtained without addition of the compound A was dispensed, without shaking (Fs=0). The results are shown in
As illustrated in
Dispensing, freezing, rewarming (thawing), and culturing were carried out with predetermined suspension times is (0 to 4 h) in the same manner as that in Test Example 3, except that the liquid reservoir bottle was not shaken (Fs=0), and a cryopreservation solution was converted to a plastic fluid by using CaCl2) and the compound A (CaCl2): 2 mM, Compound A: 0.06%). A viability γ (%) determined based on a cell count before stirring and a cell count after stirring, a viability β (%) determined based on a cell count before freezing and a cell count after rewarming (thawing), and an adherent cell ratio α (%) determined based on an adherent cell count before seeding for recultivation and an adherent cell count at 24 hours after the same were calculated. Further, a double acceleration μ (h) in recultivation was measured. These results are compared with those in a case where the compound A was not used (the solution was not converted to a plastic fluid), and are shown in
Besides, based on observation of recultivation, comparison was carried out between a case where the cryopreservation solution was converted to a plastic fluid with use of the compound A, and a case where the compound A was not added (in the case where the cryopreservation solution was not converted to a plastic fluid). The results are shown in
As illustrated in
From the above, it is recognized that the use of a plastic fluid in dispensing a cell-dispersed cryopreservation solution can suppress the unevenness of the dispensed amount for an aliquot and the unevenness of the cell density without stirring/shaking, and further, enables a dispensing operation that can suppress the unevennesses while maintaining the cell quality (viability, etc.).
Plastic fluids (SCB-GG(+) and SS-GG(+)) were produced by the same procedure in the above-described plastic fluid production, using cryopreservation solutions shown in Table 1 below, CaCl2), and the compound A (deacylated gellan gum, produced by Nissan Chemical Corporation).
In the fluids SCB-GG(+) and SS-GG(+), hiPS cells (1383D2 strain) were dispersed, and dispensing, freezing, rewarming (thawing), and culturing were carried out with predetermined suspension times is (0 to 4 h), without shaking of the liquid reservoir bottle (Fs=0). A viability γ (%) determined based on a cell count before dispensing and a cell count after dispensing, a viability β (%) determined based on a cell count before freezing and a cell count after rewarming (thawing), an adhesion rate a (%) determined based on an adherence cell count before seeding for recultivation and an adherent cell count at 24 hours after the same, and a cell potential P/P0(=α×β×γ) were calculated. The results are shown in
Performed was the same operation as that described above except that the compound A was not used (the solution was not converted to a plastic fluid, i.e., SCB-GG(−) and SS-(GG(−)) were used). The results are shown in
As illustrated in
| Number | Date | Country | Kind |
|---|---|---|---|
| 2018-153635 | Aug 2018 | JP | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/JP2019/031860 | 8/13/2019 | WO | 00 |
