The present disclosure relates to the fabrication of coatings for biosensors. More particularly, it relates to the fabrication of coating biosensors with biocompatible biopolymers.
Implantable sensors for measuring biomarkers, such as enzymatic assays, have a limited lifetime, as they are subjected to the defensive foreign body response. This response includes inflammation, recruitment of immune cells and the subsequent formation of a fibrotic capsule. This results in the loss of enzymatic activity and in turn loss of biosensing capability, as well as a dense capsule that may limit analyte diffusion, thus reducing the functional measurement window. Immune molecules also foul the electrochemical electrode surface, blocking and inactivating the electrode's redox ability. It is also the case that current enzymatic biosensor fabrication methods are difficult to scale without variability and requiring significant individual calibration.
Herein are described methods and systems to fabricate precise coatings on biosensors with biocompatible biopolymers via spincoating and curing a hydrogel. These thin, geometrically defined pullulan films have consistent pore sizing, chemical resistance, and provide a stable protective environment for enzymes.
In a first aspect of the invention, a method of fabricating a biosensor is disclosed, the method comprising: providing a wafer or other solid material with an electrode on a surface of the wafer or other solid material; placing a drop of hydrogel on the electrode; spinning the wafer, while the wafer is subjected to a partial vacuum; and heating the wafer or other solid material. Alternative to a wafer, another solid material can be used to support the electrode, such as glass, polymer, etc.
In a second aspect of the invention, a biosensor is disclosed, comprising: an electrode comprising a conductive layer over a substrate layer; and a hydrogel layer over the conductive layer, the hydrogel layer being less than 3 micrometers thick and comprising enzymes immobilized within the hydrogel layer. In some embodiments of the second aspect, the hydrogel layer is less than 1 micrometer thick. In some embodiments, the enzymes are in the oxidase family, such as glucose oxidase, lactate oxidase, uricase oxidase, alcohol oxidase, cortisol oxidase, xanthine oxidase, cholesterol oxidase, and/or sarcosine oxidase.
The details of one or more embodiments of the disclosure are set forth in the accompanying drawings and the description below. Other features, objects, and advantages will be apparent from the description, drawings, and claims.
The accompanying drawings, which are incorporated into and constitute a part of this specification, illustrate one or more embodiments of the present disclosure and, together with the description of example embodiments, serve to explain the principles and implementations of the disclosure.
Fabricating precise coatings on biosensors with biocompatible biopolymers can be accomplished via spincoating and curing a hydrogel on the electrode. By spincoating (“drop-spin”) thin, geometrically defined films can be deposited having consistent pore sizing, chemical resistance, and be a stable protective environment for enzymes immobilized therein. An example process for immobilizing enzymes in the hydrogel can be found in EPO Application No. EP21202802.1 titled HYDROGEL FOR IMMOBILIZATION OF ONE OR MORE ENZYME(S) AND METHOD FOR PREPARING THE SAME invented by Oliver Plettenburg et. al. and filed on Oct. 15, 2021.
As used herein, an electrode is a conductive layer (such as Pt), usually on a substrate (such as Si, silicon nitride, or Si/SiO2).
As used herein, a diffusion barrier is a layer used to protect the conducting metal layer from diffusion of impurities from another metal and from corrosion from the environment.
In some embodiments, the drop-spin process includes placing one or more spaced-apart drops of hydrogel (e.g., pullulan) on electrodes of a wafer, then spinning the wafer at high speed. The wafer can be placed under a vacuum to help hold the wafer to the spincoater platform (e.g., at 60-70 psi). The wafer can be held down with an adhesive in addition as an alternative. In some embodiments, the electrodes are platinum. In some embodiments, the electrodes are made of another noble metal (e.g., gold, silver), a platinum group metal, a biocompatible material like graphite or a metal such as titanium, or an oxide (e.g., SiO2, titanium oxide or Al2O3), a non-noble metal, a layer of nanoparticles or nanotubes, or other appropriate conducting material for depositing on a sensor as known in the art. In some embodiments, the process is followed by a heating step.
Hydrogels are three-dimensional networks of hydrophilic polymers. Polysaccharide polymers can be used in all applications, but other polymers may be used when the hydrogel is being used as a second protective layer. The hydrogels can comprise one or more polysaccharides differing e.g., in carbohydrate composition or molecular weight. Furthermore, the carbohydrate polymers can be functionalized to for covalent bonds with each other or with the other species. In addition, the hydrogel can be used in combination with other non-carbohydrate polymers, e.g., polyurethane layers or glutaraldehyde/albumin mixtures.
The term “hydrogel”, as used herein and in the context of the present invention, is a term being well known to a person skilled in the art and includes any network of covalently crosslinked polymer chains that are hydrophilic. It usually builds up a three-dimensional solid, consisting of hydrophilic polymer chains, being held together by specific crosslinkers. Because of the inherent crosslinkers, the structural integrity of the hydrogel network does not dissolve in water. Hydrogels are highly absorbent (they can contain over 90% water) natural or synthetic polymeric networks.
In some aspects of the invention, it may be useful to use different layers of polymers. These polymers may vary in composition, polarity, pore size and degree of crosslinking. These layers can be installed sequentially using processes described below.
In one embodiment of the invention, one or more enzymes can be added to the mixture of polymers. Furthermore, the viscosity of the resulting mixture can be adjusted by adding additional solvents, water, surfactants or other ingredients known to the one skilled in the art.
A thermally-induced, drop-spin gelation process allows application of geometrically precise layers onto sensor chip surfaces. This provides a modular fabrication system since one can control the crosslinking degree, linker polarity, linker length, and, correspondingly, the pore size. After mixing and drop-spin coating the non-viscous solutions of the individual gel components, formation of a covalent, non-degradable network can be induced in the layer by heating the sensor to mild temperatures (e.g., 40° C. for between 1 to 15 hours), which is compatible with maintaining enzymatic activity.
As used herein, a “covalent network” consists of at least two polymeric components, which are bonded together by covalent chemical bonds, i.e. not exclusively relying on e.g. electrostatic or van der Waals interactions (albeit these may contribute to forming the network). The term “non-degradable” refers to forming bonds that cannot be cleaved by enzymatic reactions (e.g., by peptidases or esterases) or autohydrolysis.
The solution can be dropped in the center of an electrode pattern set and then spun to spread across the target area. Multiple drops spread out over the pattern set can also be used. Layer thickness may be varied by changing the spin speeds (e.g., 1000-6000 rpm) with higher speeds producing thinner films. This process is compatible with microfabrication tooling, and the resulting layer is compatible with microfabrication vacuum systems and organic solvents. Thin layers between 20 nm to 1000 nm are achievable, although thicker layers can be achieved if desired. In general, thin electrode coating layers provide superior signal efficiency because diffusion time of generated reaction products to reach the electrode is shorter.
As shown herein, the drop-spin process and the various microfabrication processes allow multiple layers in multiple configurations to be built. These drop-spin hydrogels show good adhesion to repeated layers and to biosensor electrodes.
The drop-spin method is compatible with microelectronic methods for wafer processing. For examples, ultraviolet (UV) induced functionalization, vacuum, clearing/washing with organic solvents.
In the context of the present invention, the carboxymethylation degree of pullulan is presented by the expression “PCM” followed by a number (e.g. PCM1, PCM3 and PCM5). This number characterizes the respective carboxymethylation degree, meaning the carboxymethyl-groups introduced into pullulan by applying the designated number of repetitive carboxymethylation reaction cycles. As used herein, CM1, CM2, CM3, etc. describe the respective carboxymethylation degree of a polysaccharide in general (without specifically referring to pullulan).
CM1 (or in case of pullulan PCM1) is considered a low modified biopolymer. CM9 (or PCM9) is considered a highly modified biopolymer. Higher modified biopolymers (PCM5-PCM9) have a short gelation time (2-5 h; 40 mg/ml material). Low modified biopolymers (PCM1-3) have a gelation time from 3-10 h (40 mg/ml material).
Example Hydrogel
The present drop-spin method can be used with a method to immobilize enzymes in a biocompatible hydrogel that does not require a covalent binding of one or more enzyme(s) (identified in this Example as “a biocompatible hydrogel”). This hydrogel provides a perfect stabilizing environment for the enzyme, resulting in a better lifetime and enzyme stability. This hydrogel protects the enzyme from biofouling and body immune response. This hydrogel is described in EPO application No. EP21202802.1 titled HYDROGEL FOR IMMOBILIZATION OF ONE OR MORE ENZYME(S) AND METHOD FOR PREPARING THE SAME invented by Oliver Plettenburg et al. and filed on Oct. 15, 2021, and PCT/EP2022/078635 with the same title and filed on Oct. 14, 2022 and published as WO/______, all of which are incorporated by reference herein.
A method for preparing such a biocompatible hydrogel can comprise the following steps:
wherein Y is selected from the group consisting of —NH—(CH2)r-Q, —NH—(CH2CH2O)s—CH2CH2Q and —NH—(CH2—CH2—C(O))t—CH2—CH2-Q,
wherein Q is
wherein M, M′=H or Me, and
wherein W=OMe, OEt, OH, NH2 or NHMe,
The biocompatible hydrogel can comprise:
wherein Z2 is selected from the group consisting of —O—, —(CH2)r—, —NH—(CH2CH2O)s—CH2CH2— and —NH—(CH2—CH2—C(O))t—CH2—CH2—,
wherein B is
and
wherein R′ is selected from the group consisting of —CF3, —C(O)—OMe, —C(O)—OEt, —C(O)—OH, —C(O)—NH2 and —C(O)—NHMe, for non-covalent immobilization of one or more enzyme(s).
As used herein, the term “biocompatible” means, especially in connection with a hydrogel, that the respective material being called or assessed as being biocompatible has the quality of not having toxic or injurious effects on biological systems, that it has the ability to perform its desired function without eliciting any undesirable local or systemic effects in the recipient, but generating the most appropriate beneficial response in that specific situation, or the ability to exist in harmony with tissue without causing deleterious changes. Preferable properties of biocompatible materials are reduced inflammation and immunological response and/or low/limited fibrotic encapsulation.
The first and/or second polysaccharide may be optionally carboxymethylated in step b), wherein at least one OH-group of the first and/or second polysaccharide as defined herein above may be carboxymethylated. In one embodiment, the carboxymethylation is preferably carried out, when the first and/or second polysaccharide is/are pullulan or dextran.
As used herein, the term “functionalization” or “functionalized” means in general the addition of specific functional groups to afford the compound new, desirable properties, e.g. the addition of a linker unit or linker units to the existent polysaccharide structure.
Functionalization of the second polysaccharide as defined above in step c) may be with one or more linker unit(s) of the structure -A′-Y, when the monomeric repeating unit of the second polysaccharide not comprises a carboxylic acid residue, or functionalization of the second polysaccharide as defined above in step c) may be with one or more linker unit(s) of the structure -Y, when the monomeric repeating unit of the second polysaccharide comprises a carboxylic acid residue, wherein A′ is —(CH2)d—C(O)— or —C(O)—NH—, wherein d is an integer from 1 to 3, wherein Y is selected from the group consisting of —NH—(CH2)r-Q, —NH—(CH2CH2O)s—CH2CH2Q and —NH—(CH2—CH2—C(O))t—CH2—CH2-Q,
wherein Q is
wherein M, M′=H or Me, and
wherein W=OMe, OEt, OH, NH2 or NHMe.
As used in the present invention, Q may be
wherein M, M′=H or Me, and
wherein W=OMe, OEt, OH, NH2 or NHMe. If, for the structural formula
the structural formula
is used elsewherein herein, this does not mean for the latter mentioned structural formula that both M have to be the same (each H or each Me). Rather, the present invention also comprises that, in one embodiment both M can be H, in one embodiment both M can be Me, and in one embodiment one M can be H and the other M can be Me (independent from the position of M, two possibilities for one M being H and the other M being Me). Thus, in the context of the present invention, the two structural formulas
can be used interchangeably herein.
Moreover, in the context of the present invention, it is absolutely clear for the person skilled in the art, with regard to the functionalization of the second polysaccharide with one or more linker unit(s) of the structure -A′-Y,
wherein Y is selected from the group consisting of —NH—(CH2)r-Q, —NH—(CH2CH2O)s—CH2CH2Q and —NH—(CH2—CH2—C(O))t—CH2—CH2-Q,
wherein Q is
wherein M, M′=H or Me, and
wherein W=OMe, OEt, OH, NH2 or NHMe, that the linking of Q within —NH—(CH2)r-Q, —NH—(CH2CH2O)s—CH2CH2Q or —NH—(CH2—CH2—C(O))t—CH2—CH2-Q, is via the dashed line given in the structural formulas
In one embodiment, in step d), optionally the addition of one or more enzyme(s) to the mixture formed by the steps a)-c) may be carried out. In this embodiment, any enzyme is in principle possible.
In step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 25° C. to 70° C. for at least one hour. It is more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 25° C. to 70° C. for 1-15 hours. It is even more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 25° C. to 70° C. for 1-10 hours.
It is preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 30° C. to 60° C. for at least one hour. It is more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 30° C. to 60° C. for 1-15 hours. It is even more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 30° C. to 60° C. for 1-10 hours.
It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 50° C. for at least one hour. It is more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 50° C. for 1-15 hours. It is even more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 50° C. for 1-10 hours.
It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 45° C. for at least one hour. It is more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 45° C. for 1-15 hours. It is even more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 45° C. for 1-10 hours.
It is more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature of about 40° C. for at least one hour. It is even more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature of about 40° C. for 1-15 hours. It is even more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature of about 40° C. for 1-10 hours.
It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 30° C. to 60° C. for 4 to 10 hours. It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 50° C. for 4 to 10 hours. It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 45° C. for 4 to 10 hours. It is more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature of about 40° C. for 4 to 10 hours.
It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 30° C. to 60° C. for 4 to 6 hours. It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 50° C. for 4 to 6 hours. It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 45° C. for 4 to 6 hours. It is more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature of about 40° C. for 4 to 6 hours.
It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 30° C. to 60° C. for 6 to 8 hours. It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 50° C. for 6 to 8 hours. It is further preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature being in the range from 35° C. to 45° C. for 6 to 8 hours. It is more preferred that in step e), the incubation of the mixture formed by steps a)-d) is carried out in an aqueous medium at a temperature of about 40° C. for 6 to 8 hours.
This method of preparing a biocompatible hydrogel may comprise with step e) a step comprising thermo-induced gelation, which e.g. allows formation of specific form factors e.g. by complete bubble-free filling of a suitably formed mould or by dropping a mixture of the two non-viscous solutions of the individual components into a lipophilic organic medium to form droplets of defined diameter. Formation of a covalent, non-degradable network of a biocompatible hydrogel can be induced by heating to mild temperatures as described above, which is compatible with maintaining enzymatic activity, when an enzyme is encapsulated therein. The method may comprise crosslinking via 1,3-dipolar cycloaddition, thermo-gelation under very mild reaction conditions (e.g., 40° C. in aqueous media) with no side reaction and no toxic reagent (e.g. glutaraldehyde). Optimization of pore sizes of the biocompatible hydrogel is possible by feasible adjustment of parameters and adjusting the degree of optional carboxymethylation. If an enzyme is added as described in step d), the one or more enzyme(s) will be immobilized in the produced biocompatible hydrogel, wherein the one or more enzyme(s) is/are then significantly longer stable and active than the free enzyme in solution at ambient or elevated temperature, e.g. body temperature, 37° C. Unstable sensitive enzymes, like alcohol oxidase, or glucose oxidase, have better lifetime performances under these conditions. This embodiment is also applicable to other sensitive enzymes. Such a produced biocompatible hydrogel can be stored dry without losing higher amounts of enzyme activity. Further, no or little leaching of enzyme can be achieved. Such hydrogels prepared according to this method can be suspended in aqueous or organic solvents, while maintaining enzymatic activity (e.g., acetone). The viscosity of the individual components, as well as of the mixture can be easily adjusted.
In one embodiment of the method of preparing a biocompatible hydrogel, the first polysaccharide and the second polysaccharide are independently from each other selected from the group consisting of pullulan, alginate, cellulose, hyaluronan, dextran, lichenin, lentinan and mixtures thereof.
Pullulan is a polysaccharide polymer consisting of maltotriose units. Three glucose units of maltotriose are connected by an α-1,4-glycosidic bond, whereas consecutive maltotriose units are connected to each other by an α-1,6-glycosidic bond. Pullulan may be produced from starch by the fungus Aureobasidium pullulans. It may be mainly used by the cell to resist desiccation and predation. The presence of this polysaccharide also facilitates diffusion of molecules both into and out of the cell. In the context of the present invention, the respective monomeric repeating unit for pullulan has the structure of
with n being the number of said monomeric repeating unit of pullulan, and with n being an integer from 10 to 10000.
Alginic acid, also called algin, is a polysaccharide distributed widely in the cell walls of brown algae that is hydrophilic and forms a viscous gum, when being hydrated. Alginic acid is a linear copolymer with homopolymeric blocks of (1-4)-linked β-D-mannuronate (M) and its C-5 epimer α-L-guluronate (G) residues, respectively, are covalently linked together in different sequences or blocks. The monomers may appear in homopolymeric blocks of consecutive G-residues (G-blocks), consecutive M-residues (M-blocks) or alternating M- and G-residues (MG-blocks). With metals, such as sodium and calcium, its salts are known as alginates. In the context of the present invention, the respective monomeric repeating unit for alginate has the structure of
with n and m being the number of the monomeric repeating unit of alginate, and with n and m being each independently from each other an integer in the range from 10 to 10000.
Hyaluronic acid (abbreviated HA; conjugate base: hyaluronate), also called hyaluronan, is an anionic, non-sulfated glycosaminoglycan distributed widely throughout connective, epithelial and neural tissues. It is unique among glycosaminoglycans in that it is non-sulfated, forms in the plasma membrane instead of the Golgi apparatus and can be very large. Hyaluronic acid is a polymer of disaccharides, themselves composed of D-glucuronic acid and N-acetyl-D-glucosamine, linked via alternating β-(1→4) and β-(1→3) glycosidic bonds. In the context of the present invention, the respective monomeric repeating unit for hyaluronan has the structure of
with n being the number of said monomeric repeating unit of hyaluronan, and with n being an integer from 10 to 10000.
Dextran is a complex branched glucan (polysaccharide derived from the condensation of glucose). IUPAC defines dextrans as “branched poly-α-D-glucosides of microbial origin having glycosidic bonds predominantly C-1→C-6”. Dextran chains are of varying lengths (from 3 to 2000 kilodaltons). The polymer main chain consists of α-1,6-glycosidic linkages between glucose monomers, with random branches from α-1,3-linkages. This characteristic branching distinguishes a dextran from a dextrin, which is a straight chain glucose polymer tethered by α-1,4 or α-1,6-linkages. In the context of the present invention, the respective monomeric repeating unit for dextran has the structure of
with n being the number of said monomeric repeating unit of dextran, and with n being an integer from 10 to 10000.
Lichenin, also known as lichenan or moss starch, is a complex glucan occurring in certain species of lichens. It is chemically a mixed-linkage glycan, consisting of repeating glucose units linked by β-1,3- and β-1,4-glycosidic bonds. In the context of the present invention, the respective monomeric repeating unit for lichenin has the structure of
with n being the number of said monomeric repeating unit of lichenin, and with n being an integer from 10 to 10000.
Lentinan is a polysaccharide isolated from the fruit body of the shiitake mushroom. Chemically, lentinan is a β-1,3-beta-glucan with β-1,6-branching. In the context of the present invention, the respective monomeric repeating unit for lentinan has the structure of
with n being the number of said monomeric repeating unit of lentinan, and with n being an integer from 10 to 10000.
In one embodiment of the method of preparing a biocompatible hydrogel, the first and/or second polysaccharide is dextran or pullulan and carboxymethylation of at least one OH-group of dextran or pullulan is carried out in step b). It is preferred for this embodiment that the carboxymethylation of at least one OH-group of dextran or pullulan is carried out in step b) at C6 of dextran and/or pullulan. It is preferred for this embodiment that the carboxymethylation of at least one OH-group of dextran or pullulan is carried out in step b) at C2 of dextran and/or pullulan. It is preferred for this embodiment that the carboxymethylation of at least one OH-group of dextran or pullulan is carried out in step b) at C3 of dextran and/or pullulan. It is preferred for this embodiment that the carboxymethylation of at least one OH-group of dextran or pullulan is carried out in step b) at C4 of dextran and/or pullulan.
In a further embodiment of the method of preparing a biocompatible hydrogel, in step c) the first polysaccharide is functionalized with 0.01-1.5 of A per monomeric repeating unit of the first polysaccharide. In a further preferred embodiment of the method of preparing a biocompatible hydrogel, in step c) the first polysaccharide is functionalized with 0.05-1.5 of A per monomeric repeating unit of the first polysaccharide. In a further preferred embodiment of the method of preparing a biocompatible hydrogel, in step c) the first polysaccharide is functionalized with 0.05-1.0 of A per monomeric repeating unit of the first polysaccharide.
For the method of preparing a biocompatible hydrogel, it is preferred that in step c) the second polysaccharide is functionalized with 0.01-1.5 of A′ per monomeric repeating unit of the second polysaccharide. In a further preferred embodiment of the method of preparing a biocompatible hydrogel, in step c) the second polysaccharide is functionalized with 0.05-1.5 of A′ per monomeric repeating unit of the second polysaccharide. In a further preferred embodiment of the method of preparing a biocompatible hydrogel according to the present invention, in step c) the second polysaccharide is functionalized with 0.05-1.0 of A′ per monomeric repeating unit of the second polysaccharide.
In a further embodiment of the method of preparing a biocompatible hydrogel, in step c) the first polysaccharide is functionalized with 0.01-1.5 of X per monomeric repeating unit of the first polysaccharide. In a further preferred embodiment of the method of preparing a biocompatible hydrogel according to the present invention, in step c) the first polysaccharide is functionalized with 0.05-1.5 of X per monomeric repeating unit of the first polysaccharide. In a further preferred embodiment of the method of preparing a biocompatible hydrogel according to the present invention, in step c) the first polysaccharide is functionalized with 0.05-1.0 of X per monomeric repeating unit of the first polysaccharide.
It is preferred that in step c) the second polysaccharide is functionalized with 0.01-1.5 of Y per monomeric repeating unit of the second polysaccharide. In a further preferred embodiment of the method of preparing a biocompatible hydrogel, in step c) the second polysaccharide is functionalized with 0.05-1.5 of Y per monomeric repeating unit of the second polysaccharide. In a further preferred embodiment of the method of preparing a biocompatible hydrogel, in step c) the second polysaccharide is functionalized with 0.05-1.0 of Y per monomeric repeating unit of the second polysaccharide.
In one embodiment of the method of preparing a biocompatible hydrogel, d is 1.
It is further preferred for the method of preparing a biocompatible hydrogel, that step e) is a thermo-induced cycloaddition reaction between X and Y for forming a crosslinked polymer.
In one embodiment of the method of preparing a biocompatible hydrogel, the content of N3 is 0.01-1.5 N3 per monomeric repeating unit of the first polysaccharide. In one preferred embodiment of the method of preparing a biocompatible hydrogel, the content of N3 is 0.01-1.0 N3 per monomeric repeating unit of the first polysaccharide. In one further preferred embodiment of the method of preparing a biocompatible hydrogel, the content of N3 is 0.1-1.0 N3 per monomeric repeating unit of the first polysaccharide.
In one embodiment of the method of preparing a biocompatible hydrogel, the content of Q is 0.01-1.5 per monomeric repeating unit of the second polysaccharide. In one preferred embodiment of the method of preparing a biocompatible hydrogel, the content of Q is 0.01-1.0 per monomeric repeating unit of the second polysaccharide. In one preferred embodiment of the method of preparing a biocompatible hydrogel, the content of Q is 0.1-1.0 per monomeric repeating unit of the second polysaccharide.
In one preferred embodiment of the method of preparing a biocompatible hydrogel, in step c) -A-X is linked to at least one primary or secondary OH-group of the first polysaccharide, preferably via at least one of C2, C3, C4 or C6 of the monomeric repeating unit of the first polysaccharide, more preferably via C6 of the monomeric repeating unit of the first polysaccharide.
In one preferred embodiment of the method of preparing a biocompatible hydrogel, wherein in step c) -A′-Y is linked to at least one primary or secondary OH-group of the second polysaccharide, preferably via at least one of C2, C3, C4 or C6 of the monomeric repeating unit of the second polysaccharide, more preferably via C6 of the monomeric repeating unit of the second polysaccharide.
It is further preferred for the method of preparing a biocompatible hydrogel, that the method is without the use of toxic reagents, preferably without the use of glutaraldehyde.
In one embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the unfunctionalized first polysaccharide is in the range from 5 to 2000 kDa. In one embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the functionalized first polysaccharide is in the range from 5 to 2500 kDa. In one preferred embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the functionalized first polysaccharide is in the range from 5 to 2000 kDa. In one more preferred embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the functionalized first polysaccharide is in the range from 5 to 1500 kDa. In one even more preferred embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the functionalized first polysaccharide is in the range from 10 to 1500 kDa.
In one embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the unfunctionalized second polysaccharide is in the range from 5 to 2000 kDa. In one embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the functionalized second polysaccharide is in the range from 5 to 2500 kDa. In one preferred embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the functionalized second polysaccharide is in the range from 5 to 2000 kDa. In one more preferred embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the functionalized second polysaccharide is in the range from 5 to 1500 kDa. In one even more preferred embodiment of the method of preparing a biocompatible hydrogel, the molecular weight of the functionalized second polysaccharide is in the range from 10 to 1500 kDa.
The hydrogel is obtainable by any method of preparing a biocompatible hydrogel as described above. It is preferred that said hydrogel comprises one or more encapsulated enzyme(s). It is further preferred that the hydrogel is a swellable or swollen hydrogel matrix.
A number of embodiments of the disclosure have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the present disclosure. Accordingly, other embodiments are within the scope of the following claims.
The examples set forth above are provided to those of ordinary skill in the art as a complete disclosure and description of how to make and use the embodiments of the disclosure, and are not intended to limit the scope of what the inventor/inventors regard as their disclosure.
Modifications of the above-described modes for carrying out the methods and systems herein disclosed that are obvious to persons of skill in the art are intended to be within the scope of the following claims. All patents and publications mentioned in the specification are indicative of the levels of skill of those skilled in the art to which the disclosure pertains. All references cited in this disclosure are incorporated by reference to the same extent as if each reference had been incorporated by reference in its entirety individually.
It is to be understood that the disclosure is not limited to particular methods or systems, which can, of course, vary. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting. As used in this specification and the appended claims, the singular forms “a,” “an,” and “the” include plural referents unless the content clearly dictates otherwise. The term “plurality” includes two or more referents unless the content clearly dictates otherwise. Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which the disclosure pertains. The terms “over” and “under” are understood to show relative positions to other elements and not absolute positions with reference to the ground.
The present application claims priority to U.S. Provisional Patent Application No. 63/256,086 titled “Methods and Systems for Fabricating Biosensors”, filed on Oct. 15, 2021, the disclosure of which is incorporated by reference herein in its entirety.
Number | Date | Country | |
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63256086 | Oct 2021 | US |