Patent Application
20230312615
Hydrogen sulfide (H2S) is a colorless, flammable gas with a distinctive “rotten-egg” odor that is pervasive in industrial processes such as petroleum refining, natural gas processing, and wastewater treatment. Because H2S is an irritant to respiratory linings and a chemical asphyxiant, it has a recommended Immediately Dangerous to Life and Health (IDLH) value of 100 ppm, above which prolonged exposure can be fatal. In addition to being toxic to humans at high concentrations, H2S impurities in gas streams are highly corrosive to piping and other equipment. In spite of its toxic and corrosive nature, H2S is also an important gasotransmitter in mammals with proposed roles in calcium homeostasis, long-term potentiation, and mediation of oxidative stress. As such, H2S has been invoked as a potential therapeutic for numerous disorders, including bone disease, brain injury, inflammation, Parkinson's disease, high blood pressure, cancer, and ischemia-reperfusion injury.
The toxicity and flammability of H2S limit the viability of inhalation as a therapeutic delivery pathway. Indeed, studies regarding the potential biological role and therapeutic value of H2S rarely employ this gas directly. Instead, researchers have designed small molecule donors that decompose to generate H2S or related species under physiological conditions. However, the application of these donors is complicated by the concomitant production of reactive byproducts and other sulfur-based species upon H2S release. An promising alternative strategy is to design biocompatible porous solids capable of storing and controllably releasing gaseous H2S, avoiding the formation of biologically-active byproducts. In particular, metal-organic frameworks (MOFs), which are porous materials constructed from organic “linkers” and inorganic “nodes,” are potential materials for the controlled delivery of bioactive molecules. The chemical tunability of MOFs achievable through linker modification and surface functionalization is a potential feature that could potentially provide control over the rate and location of H2S delivery.
To be useful for H2S delivery in vivo, MOF-based platforms must meet several criteria, including: (1) construction from non-toxic metals and linkers; (2) stability towards H2S; (3) high H2S capacities with controlled release under physiological conditions; and (4) stability under physiological conditions (e.g., serum at 37° C.). However, none of the MOFs that have been studied for H2S adsorption to date fulfill all of these criteria, as many are limited by framework destruction upon irreversible H2S binding, low capacities, poor biocompatibility, or harsh H2S desorption conditions. In addition, many previously studied MOFs are constructed from toxic metals (e.g., Ni, Cr) or complex organic linkers that could lead to unwanted side effects in vivo. For example, the only MOF that has been explored for therapeutic H2S delivery to date, namely, Zn-MOF-74, fails to meet several of these criteria. It is known that H2S adsorption in Zn-MOF-74 is completely irreversible, which precludes its application for H2S delivery. This framework was also found to be highly toxic to HeLa cells. The controlled delivery of H2S remains an unsolved challenge in medicine and biology.
The present disclosure provides, inter alia, Zr-based metal-organic frameworks (Zr-MOFs) comprising polycarboxylate groups, methods of making one or more Zr-based (Zr-MOF(s)), hydrogen sulfide-loaded Zr-based metal-organic frameworks (H2S-loaded Zr-MOFs), methods of making one or more H2S-loaded Zr-MOF(s), and methods of H2S delivery.
In various examples, a Zr-based metal-organic framework (Zr-MOF) comprising the following formula: Zr6O4(OH)4(polycarboxylate)6. In various examples, the Zr-MOF is not Zr6O4(OH)4(fumarate)6 (Zr-fum) and/or Zr6O4(OH)4(mesaconate)6 (Zr-mes). In various examples, the polycarboxylate is independently at each occurrence a group chosen from saturated polycarboxylate groups, unsaturated polycarboxylate groups, straight-chain polycarboxylate groups, branched polycarboxylate groups, cyclic polycarboxylate groups, heterocyclic polycarboxylate groups, aromatic polycarboxylate groups, heteroaromatic polycarboxylate groups, and the like, and any combination thereof. In various examples, the Zr-MOF is completely amorphous, at least partially amorphous and/or crystalline, or completely crystalline. In various examples, the Zr-MOF comprises a plurality of pores. In various examples, the pores have a longest linear dimension perpendicular to the long axis of the pores of from about 0.1 Angstrom(s) (Å) to about 200 Å.
In various examples, a method of making one or more Zr-MOF(s) independently comprising the following formula: Zr6O4(OH)4(polycarboxylate)6 (e.g., where none of the Zr-MOF(s) is/are Zr6O4(OH)4(fumarate)6 (Zr-fum) and/or Zr6O4(OH)4(mesaconate)6 (Zr-mes)), comprises: forming a Zr-MOF reaction mixture comprising: one or more zirconium compound(s), one or more polycarboxylic acid(s), one or more polycarboxylate salt(s), or any combination thereof, one or more basic solvent(s), one or more non-basic solvents(s), or any combination thereof, and optionally, one or more acid modulator(s), heating the reaction mixture, where one or more Zr-MOF(s) is/are formed, and optionally, isolating and/or activating the Zr-MOF(s).
In various examples, a H2S-loaded Zr-MOF comprises a Zr-based metal organic framework (Zr-MOF) comprising the following formula: Zr6O4(OH)4(polycarboxylate)6 and H2S (e.g., where the Zr-MOF comprises H2S). In various examples, the H2S-loaded Zr-MOF comprises an H2S loading of from about 0 millimol H2S per gram of Zr-MOF (mmol H2S/g Zr-MOF) to about 10 mmol H2S/g Zr-MOF. In various examples, the H2S-loaded Zr-MOF is capable of releasing at least a portion of or all of the H2S comprised in the H2S-loaded Zr-MOF.
In various examples, a method of making one or more H2S-loaded Zr-MOF(s) comprises: forming an H2S-loading reaction mixture comprising: H2S, and one or more Zr-MOF(s) independently comprising the following formula: Zr6O4(OH)4(polycarboxylate)6, where the one or more Zr-MOF(s) comprising H2S (the H2S-loaded Zr-MOF(s)) is/are formed, and optionally, isolating and/or activating the H2S-loaded Zr-MOF(s). In various examples, a method further comprises (e.g., after forming the H2S-loaded Zr-MOF(s)), forming one or more desorbed Zr-MOF(s) (e.g., subjecting the H2S-loaded Zr-MOF(s) to reduced pressure, heat, an aqueous environment, a solvent, or any combination thereof, thereby forming one or more desorbed Zr-MOF(s), and optionally, isolating and/or activating the desorbed Zr-MOF(s) or the like).
In various examples, a method of H2S delivery comprises: contacting an aqueous environment, a solvent, or the like, or any combination thereof, with one or more H2S-loaded Zr-MOF(s), wherein at least a portion of or all of the H2S comprised by the H2S-loaded Zr-MOF(s) is released into the aqueous environment, the solvent, or the like, or the combination thereof, and wherein one or more desorbed Zr-MOF(s) is/are formed, and optionally, isolating and/or activating the desorbed Zr-MOF(s). In various examples, the H2S-loaded Zr-MOF(s) deliver from about 0 micromol per liter (μM) H2S to about 400 μM H2S to the aqueous environment, the solvent, or the like, or the combination thereof. In various examples, the aqueous environment is comprised within an individual or a portion of an individual. In various examples, the H2S-loaded Zr-MOF(s) is/are taken up by a cell or a population of cells, and wherein H2S is released within the cell or the population of cells. In various examples, the individual is an individual suffering from or at risk of an ischemia-reperfusion injury, inflammation, a wound, or any combination thereof, and wherein delivery treats or prevents the ischemia-reperfusion injury, the inflammation, the wound, or the combination thereof, in the individual.
The patent or application file contains at least one drawing executed in color. Copies of this patent or patent application publication with color drawing(s) will be provided by the Office upon request and payment of the necessary fee.
For a fuller understanding of the nature and objects of the disclosure, reference should be made to the following detailed description taken in conjunction with the accompanying figures.
Although claimed subject matter will be described in terms of certain examples, other examples, including examples that do not provide all of the benefits and features set forth herein, are also within the scope of this disclosure. Various structural, logical, and process step changes may be made without departing from the scope of the disclosure.
As used herein, unless otherwise indicated, “about”, “substantially”, or “the like”, when used in connection with a measurable variable (such as, for example, a parameter, an amount, a temporal duration, or the like) or a list of alternatives, is meant to encompass variations of and from the specified value including, but not limited to, those within experimental error (which can be determined by, e.g., a given data set, an art accepted standard, etc. and/or with, e.g., a given confidence interval (e.g., 90%, 95%, or more confidence interval from the mean), such as, for example, variations of +/−10% or less, +/−5% or less, +/−1% or less, and +/−0.1% or less of and from the specified value), insofar such variations in a variable and/or variations in the alternatives are appropriate to perform in the instant disclosure. As used herein, the term “about” may mean that the amount or value in question is the exact value or a value that provides equivalent results or effects as recited in the claims or taught herein. That is, it is understood that amounts, sizes, compositions, parameters, and other quantities and characteristics are not and need not be exact, but may be approximate and/or larger or smaller, as desired, reflecting tolerances, conversion factors, rounding off, measurement error, or the like, or other factors known to those of skill in the art such that equivalent results or effects are obtained. In general, an amount, size, composition, parameter, or other quantity or characteristic, or alternative is “about” or “the like,” whether or not expressly stated to be such. It is understood that where “about,” is used before a quantitative value, the parameter also includes the specific quantitative value itself, unless specifically stated otherwise.
Ranges of values are disclosed herein. The ranges set out a lower limit value and an upper limit value. Unless otherwise stated, the ranges include the lower limit value, the upper limit value, and all values between the lower limit value and the upper limit value, including, but not limited to, all values to the magnitude of the smallest value (either the lower limit value or the upper limit value) of a range. It is to be understood that such a range format is used for convenience and brevity, and thus, should be interpreted in a flexible manner to include not only the numerical values explicitly recited as the limits of the range, but also to include all the individual numerical values or sub-ranges encompassed within that range as if each numerical value and sub-range is explicitly recited. To illustrate, a numerical range of “0.1% to 5%” should be interpreted to include not only the explicitly recited values of 0.1% to 5%, but also, unless otherwise stated, include individual values (e.g., 1%, 2%, 3%, and 4%) and the sub-ranges (e.g., 0.5% to 1.1%, 0.5% to 2.4%, 0.5% to 3.2%, and 0.5% to 4.4%, and other possible sub-ranges) within the indicated range. It is also understood (as presented above) that there are a number of values disclosed herein, and that each value is also herein disclosed as “about” that particular value in addition to the value itself. For example, if the value “10” is disclosed, then “about 10” is also disclosed. Ranges can be expressed herein as from “about” one particular value, and/or to “about” another particular value. Similarly, when values are expressed as approximations, by use of the antecedent “about”, it will be understood that the particular value forms a further disclosure. For example, if the value “about 10” is disclosed, then “10” is also disclosed.
As used herein, unless otherwise indicated, the term “alkyl group” refers to branched or unbranched hydrocarbon groups that include only single bonds between carbon atoms. In various examples, an alkyl group is a C1 to C50 alkyl group, including all integer numbers of carbons and ranges of numbers of carbons therebetween (e.g., a C1, C2, C3, C4, C5, or C6,). In various examples, an alkyl group is a saturated group. In various examples, an alkyl group is a cyclic alkyl group, e.g., a monocyclic alkyl group or a polycyclic alkyl group. Examples of alkyl groups include, but are not limited to, methyl groups, ethyl groups, propyl groups, isopropyl groups, butyl groups, isobutyl groups, tert-butyl groups, benzyl groups, cyclohexyl groups, adamantyl groups, and the like. In various examples, an alkyl group is unsubstituted or substituted with one or more substituent(s). Examples of substituents include, but are not limited to, various substituents such as, for example, halide groups (—F, —Cl, —Br, and —I), hydroxyl groups, amine groups, nitro groups, cyano groups, isocyano groups, alkoxide groups, alcohol groups, ether groups, ketone groups, carboxylate groups, carboxylic acid groups, ester groups, amide groups, thioether groups, and the like, and any combination thereof.
As used herein, unless otherwise stated, the term “alkenyl group” refers to branched or unbranched hydrocarbons comprising at least one carbon-carbon double bond. Examples of alkenyl groups include, but are not limited to, ethenyl groups, propenyl groups, isopropenyl groups, butenyl groups, isobutenyl groups, tert-butenyl groups, and the like. In various examples, an alkenyl group is a C2 to C10 alkenyl group, including all integer numbers of carbons and ranges of numbers of carbons therebetween (e.g., C2, C3, C4, C5, or C6,). In various examples, an alkenyl group is a cyclic alkenyl group, e.g., a monocyclic alkenyl group or a polycyclic alkenyl group. In various examples, an alkenyl group is unsubstituted or substituted with one or more substituent(s). Examples of substituents include, but are not limited to, various substituents such as, for example, halide groups (—F, —Cl, —Br, and —I), hydroxyl groups, amine groups, nitro groups, cyano groups, isocyano groups, alkoxide groups, alcohol groups, ether groups, ketone groups, carboxylate groups, carboxylic acid groups, ester groups, amide groups, thioether groups, and the like, and any combination thereof.
As used herein, unless otherwise stated, the term “cyclic group” refers to branched or unbranched hydrocarbons, which may be saturated or unsaturated (e.g., comprising at least one carbon-carbon double bond or the like.) In various examples, a cyclic group is a monocyclic group or a polycyclic group. In various examples, a cyclic group (which may be referred to as a heterocyclic group) comprises one or more heteroatom(s) in a ring or rings, if present, of the cyclic group, such as, for example, oxygen, nitrogen (e.g., pyridinyl groups and the like), sulfur, and the like, and any combination thereof.
As used herein, unless otherwise indicated, the term “aromatic group” refers to C5 to C30 aromatic or partially aromatic carbocyclic groups, including all integer numbers of carbons and ranges of numbers of carbons therebetween (e.g., C5, C6, C7, C8, C9, C10, C11, C12, C13, C14, C15, C16, C17, C18, C19, C20, C21, C22, C23, C24, C25, C26, C27, C28, C29, and C30). In various examples, an aromatic group is a polyaromatic group, such as, for example, a polyaromatic group comprising fused aromatic rings, biaromatic (or biraryl) groups, or a combination thereof.
In various examples, an alkenyl group is unsubstituted or substituted with one or more substituent(s). Examples of substituents include, but are not limited to, various substituents such as, for example, halide groups (—F, —Cl, —Br, and —I), hydroxyl groups, amine groups, nitro groups, cyano groups, isocyano groups, alkoxide groups, alcohol groups, ether groups, ketone groups, carboxylate groups, carboxylic acid groups, ester groups, amide groups, thioether groups, and the like, and any combination thereof. Examples of aromatic groups include, but are not limited to, phenyl groups, biaryl groups (e.g., biphenyl groups and the like), fused ring groups (e.g., naphthyl groups and the like), hydroxybenzyl groups, tolyl groups, xylyl groups, furanyl groups, benzofuranyl groups, indolyl groups, imidazolyl groups, benzimidazolyl groups, pyridinyl groups, and the like. In various examples, an aromatic group (which may be referred to as a heteroaromatic group) comprises one or more heteroatom(s) in the ring or rings, if present, of the aromatic group, such as, for example, oxygen, nitrogen (e.g., pyridinyl groups and the like), sulfur, and the like, and any combination thereof. Examples of aromatic groups include, but are not limited to, phenyl groups, biaryl groups (e.g., biphenyl groups and the like), fused ring groups (e.g., naphthyl groups and the like), hydroxybenzyl groups, tolyl groups, xylyl groups, furanyl groups, benzofuranyl groups, indolyl groups, imidazolyl groups, benzimidazolyl groups, pyridinyl groups, and the like.
As used herein, unless otherwise stated, the term “group” refers to a chemical entity that is monovalent (i.e., has one terminus that can be covalently bonded to other chemical species), divalent, or polyvalent (i.e., has two or more termini that can be covalently bonded to other chemical species). The term “group” also includes radicals (e.g., monovalent radicals and multivalent radicals, such as, for example, divalent radicals, trivalent radicals, and the like). Illustrative examples of groups include:
and the like.
The present disclosure provides zirconium (Zr)-based metal-organic frameworks (Zr-MOFs). The present disclosure also provides methods of making and uses of zirconium (Zr)-based metal-organic frameworks (Zr-MOFs).
In an aspect, the present disclosure provides zirconium (Zr)-based metal-organic frameworks (Zr-MOFs). In various examples, a Zr-MOF is made by a method of the present disclosure. Non-limiting examples of Zr-MOFs are disclosed herein.
In various examples, a Zr-based metal-organic framework (Zr-MOF) comprises (or has) the following formula and/or structure: Zr6O4(OH)4(polycarboxylate)6. In various examples, the Zr6O4(OH)4(polycarboxylate)6 is Zr6O4(OH)4(itaconate)6 (Zr-ita). In various examples, the Zr6O4(OH)4(polycarboxylate)6 is not Zr6O4(OH)4(fumarate)6 (Zr-fum) or Zr6O4(OH)4(mesaconate)6 (Zr-mes).
A Zr-MOF can comprise various polycarboxylates. In various examples, a polycarboxylate (polycarboxylate group) is formed from a polycarboxylic compound or polycarboxylate compound. In various examples, a polycarboxylate (a polycarboxylate group) comprises two or more carboxylate group(s). In various examples, a polycarboxylate is independently at each occurrence chosen from dicarboxylates, tricarboxylates, tetracarboxylates, and the like. In various examples, a polycarboxylate is independently at each occurrence chosen from C2-C50 polycarboxylates, including all integer carbon number values and ranges therebetween (e.g., a C1, C2, C3, C4, C5, or C6,). In various examples, a polycarboxylate (a polycarboxylate group) comprises one or more alkyl group(s) or the like. In various examples, a polycarboxylate (a polycarboxylate group) comprises one or more alkenyl group(s), which may, independently, comprise terminal (=CH2) groups, or the like. In various examples, a polycarboxylate (a polycarboxylate group) comprises one or more aromatic group(s) or the like. In various examples, a polycarboxylate (a polycarboxylate group) comprises one or more porphyrin group(s) or the like. In various examples, a polycarboxylate (a polycarboxylate group) comprises one or more alkyl group(s), one or more alkenyl group(s), independently, comprising terminal (=CH2) groups, one or more aromatic group(s), one or more porphyrin group(s), or the like, or any combination thereof. Non-limiting examples of polycarboxylates include saturated polycarboxylates, unsaturated polycarboxylates, straight-chain polycarboxylates, branched polycarboxylates, cyclic polycarboxylates, heterocyclic polycarboxylates, aromatic polycarboxylates, and heteroaromatic polycarboxylates, and the like, and any combination thereof. In various examples, a polycarboxylate (polycarboxylate group) is independently at each occurrence chosen from carboxylates (carboxylate groups) of fumaric acid, mesaconic acid, itaconic acid, terephthalic acid, succinic acid, glutamic acid, oxalic acid, glutaric acid, 4,4′-biphenyldicarboxylic acid, 2,6-naphthalenedicarboxylic acid, trimesic acid, tetrakis(4-carboxyphenyl)porphyrin, and the like.
A Zr-MOF can comprise a plurality of crystalline and/or amorphous domains. In various examples, a Zr-MOF is completely amorphous, at least partially amorphous and/or crystalline, or completely crystalline.
A Zr-MOF can comprise various porous structures. In various examples, a Zr-MOF comprises a plurality of pores (e.g., a plurality of micropores, a plurality of mesopores, or the like, or any combination thereof), where the pores have a longest linear dimension (e.g., a diameter or the like) perpendicular to the long axis of the pores of from about 0.1 Angstrom(s) (Å) to about 200 Å, including all 0.1 Å values and ranges therebetween. In various examples, a plurality of pores comprises a plurality of micropores having a longest linear dimension of from about 0.1 Å to about 20 Å, including all 0.1 Å values and ranges therebetween, and/or a plurality of mesopores having a longest linear dimension of from about 20 Å to about 150 Å, including all 0.1 Å values and ranges therebetween.
A Zr-MOF can comprise or exhibit various properties. In various examples, a Zr-MOF comprises or exhibits one or more or all of the following: a Brunauer-Emmett-Teller (BET) Surface Area (e.g., as disclosed herein, such as, for example, 77 K N2) of from about 0 square-meter(s)/gram (m2/g) to about 1000 m2/g, including all 0.1 m2/g values and ranges therebetween (e.g., from about 1 m2/g to about 1000 m2/g, from about 5 m2/g to about 1000 m2/g, from about 10 m2/g to about 900 m2/g, from about 25 m2/g to about 800 m2/g, from about 30 m2/g to about 700 m2/g, from about 45 m2/g to about 600 m2/g, from about 60 m2/g to about 500 m2/g, from about 75 m2/g to about 400 m2/g, or from about 100 m2/g to about 300 m2/g); a Langmuir Surface Area (e.g., as disclosed herein, such as, for example, 77 K N2) of 0 m2/g to about 1400 m2/g, including all 0.1 m2/g values and ranges therebetween (e.g., from about 1 m2/g to about 1400 m2/g, from about 50 m2/g to about 1400 m2/g, from about 100 m2/g to about 1200 m2/g, from about 150 m2/g to about 1100 m2/g, from about 200 m2/g to about 1000 m2/g, from about 250 m2/g to about 900 m2/g, from about 300 m2/g to about 800 m2/g, from about 350 m2/g to about 700 m2/g, or from about 400 m2/g to about 600 m2/g); an Enthalpy of Adsorption (−ΔHads) for hydrogen sulfide (H2S) (e.g., as disclosed herein, such as, for example, as a function of isosteric H2S loading using the Clausius-Clapeyron equation, dual-site Langmuir models, and/or Langmuir-Freundlich models) of from about 0 kilojoule(s) (kJ)/mol to about 60 kJ/mol, including all 0.1 kJ/mol values and ranges therebetween (e.g., from about 1 kJ/mol to about 60 kJ/mol, 10 kJ/mol to about 60 kJ/mol, from about 20 kJ/mol to about 55 kJ/mol, from about 25 kJ/mol to about 50 kJ/mol, or from about 30 kJ/mol to about 40 kJ/mol); a H2S uptake capacity (e.g., as disclosed herein, such as, for example, at 25 degrees Celsius (° C.) and 1 bar of H2S) of from about 0 millimol H2S/gram of Zr-MOF (mmol H2S/g Zr-MOF) to about 10 mmol H2S/g Zr-MOF, including all 0.01 mmol H2S/g Zr-MOF values and ranges therebetween (e.g., from about 0.1 mmol H2S/g Zr-MOF to about 8 mmol H2S/g Zr-MOF, from about 0.25 mmol H2S/g Zr-MOF to about 6 mmol H2S/g Zr-MOF, from about 0.5 mmol H2S/g Zr-MOF to about 5 mmol H2S/g Zr-MOF, or from about 1.5 mmol H2S/g Zr-MOF to about 4.5 mmol H2S/g Zr-MOF); a H2S release rate (e.g., a time for a H2S-loaded Zr-MOF to release sufficient H2S into an aqueous environment, a solvent, or the like, or any combination thereof, to reach H2S saturation), of from about less than 30 seconds to less than about 24 hours, including all 1 second values and ranges therebetween; or a H2S cycling capacity decrease (e.g., as disclosed herein, such as, for example, the reduction of H2S uptake capacity after multiple cycles of H2S adsorption (e.g., exposure of a Zr-MOF to H2S (such as, for example, H2S gas at 30° C. and 1 bar) and H2S desorption (e.g., exposure of the H2S-loaded Zr-MOF to heat and/or vacuum (e.g., at 100° C. at less than 10 μbar)) of from about 0% to about 8%, including all 0.1% values and ranges therebetween after 10 cycles (e.g., from about 0.1% to about 8%, from about 1% to about 8%, from about 2% to about 8%, or from about 4% to about 8%).
In an aspect, the present disclosure provides methods of making Zr-MOFs. A method can make Zr-MOFs of the present disclosure. The methods are based on reaction of one or more zirconium precursor(s) with one or more polycarboxylic acid(s) and/or one or more polycarboxylate salts(s). Non-limiting examples of methods of making Zr-MOFs are disclosed herein.
In various examples, a method comprises making one or more Zr-MOF(s) independently comprising (or having) the following formula and/or structure: Zr6O4(OH)4(polycarboxylate)6 (e.g., a Zr6O4(OH)4(polycarboxylate)6 of the present disclosure).
In various examples, two or more or all of the Zr-MOFs are structurally and/or compositionally distinct. In various examples, the Zr6O4(OH)4(polycarboxylate)6 is Zr6O4(OH)4(itaconate)6 (Zr-ita). In various examples, the Zr6O4(OH)4(polycarboxylate)6 is not Zr6O4(OH)4(fumarate)6 (Zr-fum) or Zr6O4(OH)4(mesaconate)6 (Zr-mes). In various examples, the method of making the Zr-MOF(s) comprises: forming a Zr-MOF reaction mixture comprising: one or more zirconium compound(s) (e.g., ZrOC12, ZrC14, ZrO2, ZrO(NO3)2, a hydrate thereof, or the like, or any combination thereof), one or more polycarboxylic acid(s), one or more polycarboxylate salt(s) (e.g., Na salts, K salts, or the like, or any combination thereof), or the like, or any combination thereof, one or more basic solvent(s) (e.g., N,N-dimethylformamide (DMF), or the like), one or more non-basic solvents(s) (e.g., water at pH about 7.0, ethanol, methanol, or the like, or any combination thereof), or the like, or any combination thereof, and optionally, one or more acid modulator(s) or the like. In various examples, the method further comprises heating the reaction mixture (e.g., for a time and/or a temperature), where Zr-MOF(s) (e.g., of the present disclosure) is/are formed.
A method of making a Zr-MOF can use various reagents in addition to the zirconium compounds and the polycarboxylic acids and/or salt(s) thereof. Nonlimiting examples of additional reagents include solvent(s) and acid modulator(s), and the like, and combinations thereof. In various examples, the solvent(s) do not comprise basic solvent(s). Non-limiting examples of acid modulator(s) include carboxylic acids (such as, for example, formic acid, acetic acid, benzoic acid, substituted benzoic acids, trifluoroacetic acid, pivalic acid, and the like), amino acids (such as, for example, L-proline, histidine, alanine, and the like), mineral acids (such as, for example, hydrochloric acid, nitric acid, sulfuric acid, tetrafluoroboric acid, and the like), and the like, and salts thereof, and any combination thereof.
In various examples, a Zr-MOF reaction mixture comprise from about 1 equivalent(s) (eq) to about 10 eq of polycarboxylic acid(s), polycarboxylate salt(s) (e.g., sodium (Na) salts, potassium (K) salts, or the like, or any combination thereof), or the like, or any combination thereof, including all 0.1 eq values and ranges therebetween, based on the total equivalents of Zr. In various examples, a Zr-MOF reaction mixture comprise from about 0 equivalent(s) (eq) to about 200 eq of acid modulator(s), including all 0.1 eq values and ranges therebetween, based on the total equivalents of Zr.
In various examples, the polycarboxylic acid(s), the polycarboxylate salt(s) (e.g., Na salts, K salts, or the like, or any combination thereof), or the like, or any combination thereof, comprise(s) at least one itaconic acid or itaconate salt, and the solvent(s) do not comprise basic solvent(s). In various examples, the Zr6O4(OH)4(polycarboxylate)6 is a Zr604(OH)4(itaconate)6 (Zr-ita) and the solvent(s) do not comprise basic solvent(s).
In various examples, the Zr-MOF reaction mixture comprise from about 1 equivalent(s) (eq) to about 10 eq of polycarboxylic acid(s), polycarboxylate salt(s) (e.g., Na salts, K salts, or the like, or any combination thereof), or the like, or any combination thereof, including all 0.1 eq values and ranges therebetween, based on the total equivalents of Zr. In various examples, the Zr-MOF reaction mixture comprise from about 0 equivalent(s) (eq) to about 200 eq of acid modulator(s), including all 0.1 eq values and ranges therebetween, based on the total equivalents of Zr.
In various examples, the Zr-MOF reaction mixture is heated with or without stirring. In various examples, the Zr-MOF reaction mixture is heated with or without refluxing the solvent. In various examples, the Zr-MOF reaction mixture is heated at about the boiling temperature of the solvent(s) (e.g., in a high-pressure reaction vessel, under reflux, or the like).
In various examples, a method comprises various reaction conditions. In various examples, the Zr-MOF reaction mixture is heated with or without stirring. In various examples, the Zr-MOF reaction mixture is heated with or without refluxing the solvent. In various examples, a Zr-MOF reaction mixture is heated at a temperature of from about 30° C. to about 150° C., including all 0.1° C. values and ranges therebetween. In various examples, the Zr-MOF reaction mixture is heated at about the boiling temperature of the solvent(s) (e.g., in a high-pressure reaction vessel, under reflux, or the like).
In various examples, a method comprises various optional process(es). In various examples, a method optionally, further comprises isolating and/or activating the Zr-MOF(s) (e.g., as disclosed herein). In various examples, isolating Zr-MOF(s) is chosen from filtering, centrifuging, rinsing with solvent, solvent-exchanging, and desolvating the Zr-MOF(s), and the like, and any combination thereof. In various examples, rinsing with solvent and/or solvent-exchanging is performed with one or more solvent(s) chosen from alcohols (such as, for example ethanol, and the like, and any combination thereof) and the like.
In various examples, the isolating the Zr-MOF(s) is chosen from filtering, centrifuging, rinsing with solvent, solvent-exchanging, and desolvating the Zr-MOF(s), and the like, and any combination thereof. In various examples, the rinsing with solvent and/or the solvent-exchanging is performed with one or more solvent(s) chosen from alcohols (such as, for example ethanol, and the like, and any combination thereof) and the like.
In various examples, activating Zr-MOF(s) comprises heating the Zr-MOF(s) (e.g., for a time and/or a temperature and/or a pressure). In various examples, activating Zr-MOF(s) comprises heating the Zr-MOF(s) under vacuum at a temperature of from about 30° C. to about 100° C., including all 0.1° C. values and ranges therebetween, and/or at a pressure of from about 10 microbar(s) (μbar) to about 1000 millibar(s) (mbar), including all 0.1 μbar values and ranges therebetween. In various examples, activating the Zr-MOF(s) comprises heating the Zr-MOF(s), where the heating occurs under vacuum (<100 mTorr), with flowing N2, or the like, or any combination thereof. In various examples, activating the Zr-MOF(s) comprises heating the Zr-MOF(s) with flowing N2 at a temperature of from about room temperature (e.g., from about 20° C. to about 22° C. or the like) to about 100° C.
In an aspect, the present disclosure provides hydrogen sulfide-loaded Zr-MOFs (H2S-loaded Zr-MOFs). In various examples, a H2S-loaded Zr-MOF is made by a method of the present disclosure. In various examples, a H2S-loaded Zr-MOF comprises a Zr-MOF of the present disclosure and/or a Zr-MOF made by a method of the present disclosure. Non-limiting examples of hydrogen-sulfide loaded Zr-MOFs are described herein.
In various examples, a H2S-loaded Zr-MOF comprises a Zr-MOF comprising (or having) the following formula and/or structure: Zr6O4(OH)4(polycarboxylate)6 (e.g., of the present disclosure, such as, for example, according to and/or prepared by a method according to the present disclosure, such as, for example, Zr6O4(OH)4(fumarate)6 (Zr-fum), Zr6O4(OH)4(mesaconate)6 (Zr-mes), or Zr6O4(OH)4(itaconate)6 (Zr-ita)), and H2S (e.g., where the Zr-MOF comprises H2S (also known as a H2S-loaded Zr-MOF, e.g., of the present disclosure, such as, for example, as prepared by a method according to the present disclosure)).
A Zr-MOF of a H2S-loaded Zr-MOF can comprise H2S in various portions (or locations) of the Zr-MOF, by various mechanisms, in various quantities, or any combination thereof. In various examples, the H2S-loaded Zr-MOF comprises H2S bound to (e.g., disposed on, adsorbed on, or the like, such as, for example, hydrogen bonded to or the like) at least a portion of or all of a surface or a portion of or all of the surfaces of the Zr-MOF (e.g., an external surface, a pore surface, or the like, or any combination thereof). In various examples, a H2S-loaded Zr-MOF comprises an H2S loading of from about 0 millimol H2S/gram of Zr-MOF (mmol H2S/g Zr-MOF) to about 10 mmol H2S/g Zr-MOF, including all 0.1 mmol H2S/g Zr-MOF values and ranges therebetween (e.g., from about 0.1 mmol H2S/g Zr-MOF to about 8 mmol H2S/g Zr-MOF, from about 0.25 mmol H2S/g Zr-MOF to about 6 mmol H2S/g Zr-MOF, from about 0.5 mmol H2S/g Zr-MOF to about 5 mmol H2S/g Zr-MOF, or from about 1.5 mmol H2S/g Zr-MOF to about 4.5 mmol H2S/g Zr-MOF).
A H2S-loaded Zr-MOF can comprise or exhibit various properties. In various examples, a H2S-loaded Zr-MOF is capable of releasing (e.g., desorbing or the like) at least a portion of or all of the H2S comprised in the H2S-loaded Zr-MOF. In various examples, a H2S-loaded Zr-MOF exhibits a H2S cycling capacity decrease after 10 cycles (e.g., a cycle as disclosed herein, such as, for example, exposure of a Zr-MOF to 30° C. and 1 bar of H2S (e.g., adsorption) followed by exposure of the H2S-loaded Zr-MOF to 100° C. under vacuum (<10 μbar)(e.g., desorption)) of from about 0% to about 8%, including all 0.1% values and ranges therebetween (e.g., from about 0.1% to about 8%, from about 1% to about 8%, from about 2% to about 8%, or from about 4% to about 8%). In various examples, a H2S-loaded Zr-MOF exhibits a H2S release rate into an aqueous environment (e.g., the time required for a H2S-loaded Zr-MOF as disclosed herein to release sufficient H2S to saturate the aqueous environment) of from about less than 30 seconds to less than about 24 hours, including all 1 second values and ranges therebetween.
In an aspect, the present disclosure provides methods of making H2S-loaded Zr-MOFs. A method can make H2S-loaded Zr-MOFs of the present disclosure. The methods are based on reaction of Zr-MOFs with H2S. In various examples, methods use one or more Zr-MOF(s) of the present disclosure and/or one or more Zr-MOF(s) prepared by methods of the present disclosure. Non-limiting examples of methods of making H2S-loaded Zr-MOFs are disclosed herein.
In various examples, a method of making one or more H2S-loaded Zr-MOF(s) comprises: forming an H2S-loading reaction mixture comprising: H2S, and one or more Zr-MOF(s) independently comprising (or having) the following formula and/or structure: Zr6O4(OH)4(polycarboxylate)6 (e.g., as disclosed herein). In various examples, two or more or all of the H2S-loaded Zr-MOFs are structurally and/or compositionally distinct. In various examples, the Zr6O4(OH)4(polycarboxylate)6 is Zr6O4(OH)4(fumarate)6 (Zr-fum), Zr6O4(OH)4(mesaconate)6 (Zr-mes), Zr6O4(OH)4(itaconate)6 (Zr-ita), or any combination thereof (e.g., according to the present disclosure and/or prepared by a method according to the present disclosure).
A method of making H2S-loaded Zr-MOF(s) can comprise various reagents and ratios thereof. In various examples, H2S-loaded MOF(s) comprise(s) H2S bound to (e.g., disposed on, adsorbed on, or the like, such as, for example, hydrogen bonded to or the like) at least a portion of or all of a surface or a portion of or all of the surfaces of the Zr-MOF (e.g., an external surface, a pore surface, or the like, or any combination thereof)). In various examples, the H2S-loading reaction mixture comprises H2S in the gas phase, a solution phase (e.g., as a solution in an organic solvent, such as, for example, tetrahydrofuran or the like), or the like, or any combination thereof. In various examples, the H2S-loading reaction mixture comprise from about 1 equivalent(s) (eq) to about 100 eq of H2S, including all 0.1 eq values and ranges therebetween, based on the total equivalents of Zr.
A method of making H2S-loaded Zr-MOF(s) can comprise various reaction conditions. In various examples, a H2S-loading reaction mixture is formed with or without stirring. In various examples, Zr-MOF(s) can be dosed with H2S incrementally.
In various examples, a method of making H2S-loaded Zr-MOF(s) comprises various optional process(es). In various examples, the method further comprises isolating and/or activating the H2S-loaded Zr-MOF(s) (e.g., as disclosed herein). In various examples, Zr-MOF(s) will be desolvated and/or activated before H2S dosing.
In various examples, isolating H2S-loaded Zr-MOF(s) comprises filtering, centrifuging, rinsing with solvent, solvent-exchanging, or desolvating the H2S-loaded Zr-MOF(s), or the like, or any combination thereof. In various examples, rinsing with solvent and/or the solvent-exchanging is performed with one or more solvent(s) chosen from alcohols (such as, for example ethanol, and the like, and any combination thereof) and the like.
In various examples, activating H2S-loaded Zr-MOF(s) comprises heating the H2S-loaded Zr-MOF(s) (e.g., for a time and/or a temperature and/or a pressure). In various examples, activating H2S-loaded Zr-MOF(s) comprises heating the H2S-loaded Zr-MOF(s) under vacuum at a temperature of from about 30° C. to about 100° C., including all 0.1 ° C. values and ranges therebetween, and/or at a pressure of from about 10 microbar(s) (μbar) to about 1000 millibar(s) (mbar), including all 0.1 μbar values and ranges therebetween. In various examples, activating H2S-loaded Zr-MOF(s) comprises heating the H2S-loaded Zr-MOF(s), where the heating occurs under vacuum (<100 mTorr), with flowing N2, or the like, or any combination thereof. In various examples, activating H2S-loaded Zr-MOF(s) comprises heating the H2S-loaded MOF(s) with flowing N2 at a temperature of from about room temperature (e.g., from about 20° C. to about 22° C. or the like) to about 100° C. In various examples, Zr-MOF(s) will be dosed with H2S prior to activation.
In various examples, the present disclosure provides methods of desorbing H2S from
H2S-loaded Zr-MOF(s) of the present disclosure to make desorbed Zr-MOF(s). In various examples, desorbed Zr-MOF(s) is/are used to make H2S-MOF(s) of the present disclosure. In various examples, a method of making desorbed Zr-MOF(s) further comprises, after forming the H2S-loaded Zr-MOF(s), forming a desorbed Zr-MOF(s), the method comprising: subjecting the H2S-loaded Zr-MOF(s) to reduced pressure, heat, an aqueous environment, a solvent, or any combination thereof, thereby forming one or more desorbed Zr-MOF(s), and optionally, isolating and/or activating the desorbed Zr-MOF(s) (e.g., as disclosed herein).
In various examples, desorbed Zr-MOF(s) is/are formed by the removal of at least a portion of, substantially all, or all (e.g., at least about 20%, at least about 30%, at least about 40%, at least about 50%, at least about 60%, at least about 70%, at least about 80%, at least about 90%, or about 100%) of the H2S from H2S-loaded Zr-MOF(s). In various examples, desorbed Zr-MOF(s) is/are formed by subjecting H2S-loaded Zr-MOF(s) to a reduced pressure of from about 10 microbar (μbar) to about 1000 millibar (mbar), including all 0.1 μbar values and ranges therebetween, at a temperature of from about 25° C. to about 100° C., including all 0.1 ° C. values and ranges therebetween. In various examples, desorbed Zr-MOF(s) is/are formed by subjecting H2S-loaded Zr-MOF(s) to a reduced pressure of less than about 10 mbar at 25 ° C., less than about 10 μbar at 100° C., less than about 1000 mbar at 100° C., or the like.
Desorbed Zr-MOF(s) can comprise various properties. In various examples, a cycle of adsorption of H2S onto Zr-MOF(s) and desorption of H2S from H2S-loaded Zr-MOF(s) can be repeated for up to about 10 cycles without a substantial reduction in H2S uptake capacity of the desorbed Zr-MOF(s). In various examples, the desorbed Zr-MOF(s) exhibit(s) a H2S uptake capacity decrease after about 10 cycles (e.g., as disclosed herein, such as, for example, exposure at about 30° C. and about 1 bar of H2S and desorption at 100 ° C. under vacuum (<about 10 μbar)) of from about 4% to about 8%, including all 0.1% values and ranges therebetween (e.g., from about 0.1% to about 8%, from about 1% to about 8%, from about 2% to about 8%, or from about 4% to about 8%). H2S-loaded Zr-MOF(s) can comprise various additional process(es). In various examples, isolating desorbed Zr-MOF(s) comprises filtering, centrifuging, rinsing with solvent, solvent-exchanging, or desolvating the desorbed MOF(s), or the like, or any combination thereof. In various examples, rinsing with solvent and/or the solvent-exchanging is performed with one or more solvent(s) chosen from alcohols (such as, for example ethanol, and the like, and any combination thereof) and the like.
In various examples, activating desorbed Zr-MOF(s) comprises heating the desorbed Zr-MOF(s) (e.g., for a time and/or a temperature and/or a pressure). In various examples, activating desorbed Zr-MOF(s) comprises heating the desorbed Zr-MOF(s) under vacuum at a temperature of from about 30° C. to about 100° C., including all 0.1° C. values and ranges therebetween, and/or at a pressure of from about 10 microbar(s) (μbar) to about 1000 millibar(s) (mbar), including all 0.1 μbar values and ranges therebetween. In various examples, the activating the desorbed Zr-MOF(s) comprises heating the desorbed Zr-MOF(s), where the heating occurs under vacuum (<100 mTorr), with flowing N2, or the like, or any combination thereof. In various examples, activating the desorbed Zr-MOF(s) comprises heating the desorbed Zr-MOF(s) with flowing N2 at a temperature of from about room temperature (e.g., from about 20° C. to about 22° C. or the like) to about 100° C., including all 0.1° C. values and ranges therebetween.
In an aspect, the present disclosure provides methods of delivery of H2S. In various examples, methods use H2S-loaded Zr-MOF(s) of the present disclosure and/or H2S-loaded Zr-MOF(s) prepared by methods of the present disclosure. Non-limiting examples of methods of delivery of H2S are disclosed herein.
In various examples, a method of delivery of H2S comprises: contacting an aqueous environment, a solvent (e.g., tetrahydrofuran, ethanol, dimethyl sulfoxide, or the like, or any combination thereof), or the like, or any combination thereof, with one or more H2S-loaded Zr-MOF(s) (e.g., as disclosed herein, such as, for example, according to the present disclosure and/or prepared by a method according to the present disclosure), where at least a portion of or all of the H2S comprised by the H2S-loaded Zr-MOF(s) is released into the aqueous environment, the solvent, or the like, or any combination thereof, and where desorbed Zr-MOF(s) is/are formed (e.g., as disclosed herein, such as for example, according to the present disclosure), and optionally, isolating and/or activating the desorbed Zr-MOF(s) (e.g., as disclosed herein).
A method of delivery of H2S can deliver various H2S concentrations. In various examples, H2S-loaded Zr-MOF(s) (e.g., about 0.1 mg H2S-loaded Zr-MOF(s)/mL or less) deliver from about 0 micromol per liter (μM) H2S to about 400 μM H2S to the aqueous environment, the solvent, or the like, or any combination thereof (e.g., from about 0.1 μM H2S to about 400 μM H2S, from about 0.1 μM H2S to about 300 μM H2S, from about 0.1 μM H2S to about 200 μM H2S, from about 0.1 μM H2S to about 100 μM H2S, or from about 0.1 μM H2S to about 50 μM H2S, or about 50 μM H2S, about 100 μM H2S, about 200 μM H2S, about 300 μM H2S, or about 400 μM H2S). Non-limiting examples of aqueous environments include deionized water (such as, for example, neutral deionized water and the like), buffered saline (such as, for example, phosphate buffered saline (PBS) and the like), cell culture medium, fetal bovine serum (FBS), and the like, and any combination thereof. In various examples, H2S-loaded Zr-MOF(s) is/are contacted with the aqueous environment, the solvent, or the like, or any combination thereof, at room temperature, physiological conditions (e.g., about 37° C., or the like), 100° C., or the like. In various examples, H2S-loaded Zr-MOF(s) is/are subjected to the aqueous environment, the solvent, or the like, or any combination thereof, at a temperature of from about 25° C. to about 100° C., including all 0.1° C. values and ranges therebetween.
In various examples, aqueous environment is disposed within an individual or is a portion of an individual (e.g., cells, tissue, blood, plasma, or the like, or any combination thereof). In various examples, contacting of the portion of an individual with the H2S-loaded Zr-MOF(s) occurs outside of the individual or within the individual. In various examples, a portion of the individual contacted with the H2S-loaded Zr-MOF(s) outside of the individual is reintroduced into the individual. In various examples, a H2S-loaded Zr-MOF(s) is/are taken up by a cell or a population of cells, and where H2S is released within the cell or the population of cells. In various examples, a cell or the population of cells exhibits greater than about 50% viability (e.g., about 50% or greater, about 60% or greater, about 70% or greater, about 80% or greater, about 90% or greater, or about 100%) after the contacting of the cell or the population of cells with about 1 mg/ml or less of H2S-loaded Zr-MOF(s).
A method can be used to treat or prevent various conditions. In various examples, an individual is an individual suffering from (or at risk of) an ischemia-reperfusion injury (which may also be referred to as reperfusion injury, reoxygenation injury, hypoxia-ischemia injury, hypoxia-reoxygenation injury, or the like), inflammation (e.g., acute or chronic inflammation, local or systemic inflammation, or the like, or any combination thereof), a wound (e.g., an abrasion, a laceration, a puncture, an avulsion, or the like, or any combination thereof), or the like, or any combination thereof. In various examples, delivery of H2S to the individual treats or prevents the ischemia-reperfusion injury, the inflammation, the wound, or the like, or any combination thereof, in the individual.
In various examples, an individual is an individual suffering from (or at risk of) developing a disease or condition is an individual diagnosed with a disease or condition, an individual exhibiting one or more symptoms or indicators (e.g., markers or the like) for the disease or condition, an individual having a predisposition for (e.g., genetic factors, co-morbidities, or the like, or any combination thereof) developing the disease or condition, or the like, or any combination thereof. In various examples, an individual is an individual suffering from (or at risk of) developing an ischemia-reperfusion injury has been diagnosed with, exhibits one or more symptoms of, has a predisposition for, or the like, or any combination thereof, one or more or all of the following: a stroke, a myocardial infarction, an organ transplantation, or the like.
In various examples, desorbed Zr-MOF(s) is/are isolated (e.g., from an individual, a portion of an individual, a cell, a population of cells, or the like) and/or activated. In various examples, isolated and/or activated desorbed Zr-MOF(s) are used to make one or more H2S-loaded Zr-MOF(s) (e.g., as disclosed herein, such as, for example, according to the present disclosure or prepared by a method according to the present disclosure). In various examples, a cycle of adsorption of H2S onto Zr-MOF(s) and desorption of H2S from H2S-loaded Zr-MOF(s) can be repeated for up to about 10 without a substantial reduction in H2S uptake capacity of the desorbed Zr-MOF(s). In various examples, the desorbed Zr-MOF(s) exhibit(s) a H2S uptake capacity decrease after about 10 cycles (e.g., as disclosed herein, such as, for example, exposure at about 30° C. and about 1 bar of H2S and desorption at 100° C. under vacuum (<about 10 μbar)) of from about 4% to about 8%, including all 0.1% values and ranges therebetween (e.g., from about 0.1% to about 8%, from about 1% to about 8%, from about 2% to about 8%, or from about 4% to about 8%).
In various examples, isolating desorbed Zr-MOF(s) (e.g., from an individual, a portion of an individual, a cell, a population of cells, or the like) comprises filtering, centrifuging, rinsing with solvent, solvent-exchanging, or desolvating the desorbed Zr-MOF(s) (e.g., from the individual, the portion of an individual, the cell, the population of cells, or the like, or any combination thereof). In various examples, rinsing with solvent and/or the solvent-exchanging is performed with one or more solvent(s) chosen from alcohols (such as, for example ethanol, and the like, and any combination thereof) and the like.
In various examples, activating desorbed Zr-MOF(s) comprises heating the desorbed Zr-MOF(s) (e.g., for a time and/or a temperature and/or a pressure). In various examples, activating desorbed Zr-MOF(s) comprises heating the desorbed Zr-MOF(s) under vacuum at a temperature of from about 30° C. to about 100° C., including all 0.1° C. values and ranges therebetween, and/or at a pressure of from about 10 microbar(s) (μbar) to about 1000 millibar(s) (mbar), including all 0.1 μbar values and ranges therebetween. In various examples, activating desorbed Zr-MOF(s) comprises heating the desorbed Zr-MOF(s), where the heating occurs under vacuum (<100 mTorr), with flowing N2, or the like, or any combination thereof. In various examples, activating the desorbed Zr-MOF(s) comprises heating the desorbed Zr-MOF(s) with flowing N2 at a temperature of from about room temperature (e.g., from about 20° C. to about 22° C. or the like) to about 100° C.
A method of delivery of H2S to an individual may comprise administering one or more H2S-loaded Zr-MOF(s) of the present disclosure to the individual (which may be an effective amount of the H2S-loaded Zr-MOF(s)).
H2S-loaded Zr-MOF(s)) can be administered to an individual in need thereof via any suitable method or route to an individual in need thereof. Suitable administration routes can include, but are not limited to, auricular (otic), buccal, conjunctival, cutaneous, dental, electro-osmosis, endocervical, endosinusial, endotracheal, enteral, epidural, extra-amniotic, extracorporeal, hemodialysis, infiltration, interstitial, intra-abdominal, intra-amniotic, intra-arterial, intra-articular, intrabiliary, intrabronchial, intrabursal, intracardiac, intracartilaginous, intracaudal, intracavernous, intracavitary, intracerebral, intracisternal, intracorneal, intracoronal (dental), intracoronary, intracorporus cavernosum, intradermal, intradiscal, intraductal, intraduodenal, intradural, intraepidermal, intraesophageal, intragastric, intragingival, intraileal, intralesional, intraluminal, intralymphatic, intramedullary, intrameningeal, intramuscular, intraocular, intraovarian, intrapericardial, intraperitoneal, intrapleural, intraprostatic, intrapulmonary, intrasinal, intraspinal, intrasynovial, intratendinous, intratesticular, intrathecal, intrathoracic, intratubular, intratumor, intratympanic, intrauterine, intravascular, intravenous, intravenous bolus, intravenous drip, intraventricular, intravesical, intravitreal, iontophoresis, irrigation, laryngeal, nasal, nasogastric, occlusive dressing technique, ophthalmic, oral, oropharyngeal, other, parenteral, percutaneous, periarticular, peridural, perineural, periodontal, rectal, respiratory (inhalation), retrobulbar, soft tissue, subarachnoid, subconjunctival, subcutaneous, sublingual, submucosal, topical, transdermal, transmucosal, transplacental, transtracheal, transtympanic, ureteral, urethral, and/or vaginal administration, and/or any combination of the above administration routes, which typically depends on the condition to be treated and/or the active ingredient(s).
An individual (e.g., an individual in need of treatment or the like) may be a human or non-human mammal or other animal. Non-limiting examples of non-human mammals include cows, pigs, mice, rats, rabbits, cats, dogs, and other agricultural mammals, pets (such as, for example, dogs, cats, and the like), service animals, and the like.
“Treating” or “treatment” of any condition refers, in various examples, to ameliorating (e.g., arresting, reversing, alleviating, modulating, or the like) the condition, or reducing the manifestation, extent or severity of one or more clinical symptom(s) thereof, or the like. In various other examples, “treating” or “treatment” refers to ameliorating one or more physical parameter(s), which, independently, may or may not be discernible by the individual. In yet other examples, “treating” or “treatment” refers to modulating the condition, either physically, (e.g., stabilization of one or more discernible symptom(s), or the like), physiologically, (e.g., stabilization of one or more physical parameter, or the like), or both. In yet other examples, treating” or “treatment” relates to slowing the progression of the condition. Treating may include administration of an effective amount of the H2S-loaded Zr-MOF(s).
Typically, H2S-loaded Zr-MOF(s) is/are administered in an amount effective to treat a condition, or potential condition as described herein. As used herein, the term “effective amount” means that amount of H2S-loaded Zr-MOF(s) that will elicit the biological or medical response in an individual that is being sought, for instance, by a researcher, clinician, or the like. Effective doses of the H2S-loaded Zr-MOF(s) required to treat the progress of the medical condition are readily ascertained by one of ordinary skill in the art using preclinical and clinical approaches familiar to the medicinal arts.
A physician or veterinarian having ordinary skill in the art can readily determine and prescribe the effective amount of H2S-loaded Zr-MOF(s) required. The selected dosage level can depend upon a variety of factors including, but not limited to, the activity of the particular H2S-loaded Zr-MOF(s) employed, the time of administration, the rate of excretion or metabolism of the particular H2S-loaded Zr-MOF(s) being employed, the rate and extent of absorption, the duration of the treatment, other drugs, compounds and/or materials used in combination with the particular H2S-loaded Zr-MOF(s) employed, the age, sex, weight, condition, general health and prior medical history of an individual being treated, and like factors well known in the medical arts. For example, the physician or veterinarian could start doses of the H2S-loaded Zr-MOF(s) employed at levels lower than that required in order to achieve the desired therapeutic effect and gradually increase the dosage until the desired effect is achieved.
An effective amount may be a therapeutically effective amount. The term “therapeutically effective amount” includes any amount which, as compared to a corresponding subject who has not received such amount, results in improved treatment, healing, prevention, or amelioration of a disease, disease state, condition, disorder, side effect, or the like or a decrease in the rate of advancement of a disease, disease state, condition, disorder, or the like, or the like. he term also includes within its scope amounts effective to enhance normal physiological function.
An effective amount may result in prophylaxis. The term “prophylaxis” includes prevention and refers to a measure or procedure which is to prevent rather than cure or treat a condition. Preventing may refer to a reduction in risk of acquiring or developing a condition causing at least one clinical symptom of the condition not to develop in an individual that may be exposed to a condition causing agent or a subject predisposed to the condition in advance of condition onset.
The following Statements describe various examples of MOFs, compositions, and methods of the present disclosure and are not intended to be in any way limiting:
Statement 1. A Zr-based metal organic framework (Zr-MOF) comprising (or having) the following formula and/or structure: Zr6O4(OH)4(polycarboxylate)6, excluding Zr6O4(OH)4(fumarate)6 (Zr-fum) or Zr6O4(OH)4(mesaconate)6 (Zr-mes).
Statement 2. A Zr-based metal organic framework (Zr-MOF) according to Statement 1, where the polycarboxylate is independently at each occurrence chosen from saturated, unsaturated, straight-chain, branched, cyclic, heterocyclic, aromatic, and heteroaromatic polycarboxylates, and the like, and any combination thereof.
Statement 3. A Zr-based metal organic framework (Zr-MOF) according to Statement 1 or Statement 2, where the polycarboxylate is independently at each occurrence chosen from carboxylates of fumaric acid, mesaconic acid, itaconic acid, terephthalic acid, succinic acid, glutamic acid, oxalic acid, glutaric acid, 4,4′-biphenyldicarboxylic acid, 2,6-naphthalenedicarboxylic acid, trimesic acid, tetrakis(4-carboxyphenyl)porphyrin, and the like.
Statement 4. A Zr-based metal organic framework (Zr-MOF) according to any one of Statements 1-3, where the Zr-MOF is completely amorphous, at least partially amorphous and/or crystalline, or completely crystalline.
Statement 5. A Zr-based MOF according to any one of Statements 1-4, where the Zr-MOF comprises a plurality of pores (e.g., a plurality of micropores, a plurality of mesopores, or the like, or any combination thereof), where the pores have a longest linear dimension (e.g., a diameter or the like) perpendicular to the long axis of the pores of from about 0.1 Angstrom(s) (Å) to about 200 Å, including all 0.1 Å values and ranges therebetween.
Statement 6. A Zr-based metal organic framework (Zr-MOF) according to any one of Statements 1-5, where the Zr-MOF comprises or exhibits one or more or all of the following: a Brunauer-Emmett-Teller (BET) Surface Area (e.g., as disclosed herein, such as, for example, 77 K N2) of from about 0 square-meter(s)/gram (m2/g) to about 1000 m2/g, including all 0.1 m2/g values and ranges therebetween; a Langmuir Surface Area (e.g., as disclosed herein, such as, for example, 77 K N2) of 0 m2/ to about 1400 m2/g, including all 0.1 m2/g values and ranges therebetween; an Enthalpy of Adsorption (-Aliads) for hydrogen sulfide (H2S) (e.g., as disclosed herein, such as, for example, as a function of isosteric H2S loading using the Clausius-Clapeyron equation, dual-site Langmuir models, and/or Langmuir-Freundlich models) of from about 0 kilojoule(s) (kJ)/mol to about 60 kJ/mol, including all 0.1 kJ/mol values and ranges therebetween; a H2S uptake capacity (e.g., as disclosed herein, such as, for example, at 25° C. and 1 bar of H2S) of from about 0 millimol H2S/gram of Zr-MOF (mmol H2S/g Zr-MOF) to about 10 mmol H2S/g Zr-MOF, including all 0.01 mmol H2S/g Zr-MOF values and ranges therebetween; a H2S release rate (e.g., a time for a H2S-loaded Zr-MOF to release sufficient H2S into an aqueous environment, a solvent, or the like, or any combination thereof, to reach H2S saturation), of from about less than 30 seconds to less than about 24 hours, including all 1 second values and ranges therebetween; or a H2Scycling capacity decrease (e.g., as disclosed herein, such as, for example, the reduction of H2S uptake capacity after multiple cycles of H2S adsorption (e.g., exposure of a Zr-MOF to H2S(such as, for example, H2S gas at 30° C. and 1 bar) and H2S desorption (e.g., exposure of the H2S-loaded Zr-MOF to heat and/or vacuum (e.g., at 100° C. at less than 10 μbar)) of from about 0% to about 8%, including all 0.1% values and ranges therebetween after 10 cycles.
Statement 7. A method of making one or more Zr-based metal organic framework(s) (Zr-MOF(s)) independently comprising (or having) the following formula and/or structure: Zr6O4(OH)4(polycarboxylate)6 (e.g., a Zr6O4(OH)4(polycarboxylate)6 of the disclosure, such as, for example, according to any one of Statements 1-6), excluding Zr6O4(OH)4(fumarate)6 (Zr-fum) or Zr6O4(OH)4(mesaconate)6 (Zr-mes), the method comprising: forming a Zr-MOF reaction mixture comprising: one or more zirconium compound(s) (e.g., ZrOCl2, ZrCl4, ZrO2, ZrO(NO3)2, a hydrate thereof, or the like, or any combination thereof), one or more polycarboxylic acid(s), one or more polycarboxylate salt(s) (e.g., Na salts, K salts, or the like, or any combination thereof), or the like, or any combination thereof, one or more basic solvent(s) (e.g., N,N-dimethylformamide (DMF), or the like), one or more non-basic solvents(s) (e.g., water at pH about 7.0, ethanol, methanol, or the like, or any combination thereof), or the like, or any combination thereof, and optionally, one or more acid modulator(s) or the like, heating the reaction mixture (e.g., for a time and/or a temperature and/or a pressure), where one or more Zr-MOF(s) is/are formed, and optionally, isolating and/or activating the Zr-MOF(s) (e.g., as disclosed herein).
Statement 8. A method according to Statement 7, where the acid modulator(s) is/are chosen from: carboxylic acids (such as, for example, formic acid, acetic acid, benzoic acid, substituted benzoic acids, trifluoroacetic acid, pivalic acid, and the like), amino acids (such as, for example, L-proline, histidine, alanine, and the like), mineral acids (such as, for example, hydrochloric acid, nitric acid, sulfuric acid, tetrafluoroboric acid, and the like), and the like, and any combination thereof.
Statement 9. A method according to Statement 7 or Statement 8, where the Zr-MOF reaction mixture is heated at a temperature of from about 30 degrees Celsius (° C.) to about 150° C., including all 0.1° C. values and ranges therebetween.
Statement 10. A hydrogen sulfide-loaded Zr-based metal organic framework (H2S-loaded Zr-MOF) comprising a Zr-based metal organic framework (Zr-MOF) comprising (or having) the following formula and/or structure: Zr6O4(OH)4(polycarboxylate)6 (e.g., of the present disclosure, such as, for example, according to any one of Statements 1-6, such as, for example, as prepared by a method according to any one of Statements 7-9, such as, for example, Zr6O4(OH)4(fumarate)6 (Zr-fum), Zr6O4(OH)4(mesaconate)6 (Zr-mes), or Zr6O4(OH)4(itaconate)6 (Zr-ita)), where the Zr-MOF comprises H2S (also known as a H2S-loaded Zr-MOF, e.g., of the present disclosure, such as, for example, as prepared by a method according to Statement 14). Statement 11. A H2S-loaded Zr-MOF according to Statement 10, where the Zr-MOF comprises an H2S loading of from about 0 millimol H2S per gram of Zr-MOF (mmol H2S/g Zr-MOF) to about 10 mmol H2S/g Zr-MOF, including all 0.1 mmol H2S/g Zr-MOF values and ranges therebetween.
Statement 12. A H2S-loaded Zr-MOF according to Statement 10 or 11, where the Zr-MOF is capable of releasing (e.g., desorbing or the like) at least a portion of or all of the H2S comprised in the H2S-loaded Zr-MOF.
Statement 13. A H2S-loaded Zr-MOF according to any one of Statements 10-12, where the H2S-loaded Zr-MOF exhibits a H2S cycling capacity decrease after 10 cycles (e.g., exposure of a Zr-MOF to 30° C. and 1 bar of H2S(e.g., adsorption) followed by exposure of the H2S-loaded Zr-MOF to 100° C. under vacuum (<10 μbar)(e.g., desorption)) of from about 0% to about 8%, including all 0.1% values and ranges therebetween.
Statement 14. A method of making one or more hydrogen sulfide-loaded metal organic framework(s) (H2S-loaded Zr-MOF(s)), the method comprising: forming an H2S-loading reaction mixture comprising: H2S, and one or more Zr-MOF(s) independently comprising (or having) the following formula(s) and/or structure(s): Zr6O4(OH)4(polycarboxylate)6 (e.g., of the present disclosure, such as, for example, according to any one of Statements 1-6, such as, for example, as prepared by a method according to any one of Statements 7-9, such as, for example, Zr6O4(OH)4(fumarate)6 (Zr-fum), Zr6O4(OH)4(mesaconate)6 (Zr-mes), or Zr6O4(OH)4(itaconate)6 (Zr-ita)), where one or more Zr-MOF(s) comprising H2S is/are formed (also known as H2S-loaded Zr-MOF(s), e.g., of the present disclosure, such as, for example, according to any one of Statements 10-13), and optionally, isolating and/or activating the H2S-loaded Zr-MOF(s) (e.g., as disclosed herein).
Statement 15. A method according to Statement 14, further comprising, after the forming the H2S-loaded Zr-MOF(s), forming one or more desorbed Zr-MOF(s), the method comprising: subjecting the H2S-loaded Zr-MOF(s) to reduced pressure, heat, an aqueous environment, a solvent, or any combination thereof, thereby forming one or more desorbed Zr-MOF(s), and optionally, isolating and/or activating the desorbed Zr-MOF(s) (e.g., as disclosed herein). In various examples, one or more desorbed Zr-MOF(s) is/are used to make one or more H2S-loaded Zr-MOF(s) of the present disclosure, such as, for example, according to any one of Statement 10-13 or prepared by a method according to Statement 14.
Statement 16. A method of delivery of H2S, the method comprising: contacting an aqueous environment, a solvent (e.g., tetrahydrofuran, ethanol, dimethyl sulfoxide, or the like, or any combination thereof), or the like, or any combination thereof, with one or more H2S-loaded Zr-MOF(s) (e.g., as disclosed herein, such as, for example, according to any one of Statement 10-13 or prepared by a method according to Statement 14), where at least a portion of or all of the H2S comprised by the H2S-loaded Zr-MOF(s) is released into the aqueous environment, the solvent, or the like, or any combination thereof, and where one or more desorbed Zr-MOF(s) is/are formed (e.g., as disclosed herein, such as for example, according to Statement 15), and optionally, isolating and/or activating the desorbed Zr-MOF(s) (e.g., as disclosed herein).
Statement 17. A method according to Statement 16, where H2S-loaded Zr-MOF(s) (e.g., less than 0.1 mg H2S-loaded Zr-MOF(s)/mL or the like) deliver from about 0 micromol per liter (μM) H2S to about 400 μM H2S, including all 0.1 μM H2S values and ranges therebetween (e.g., from about 0.1 μM H2S to about 200 μM H2S or the like), to the aqueous environment, the solvent, or the like, or any combination thereof.
Statement 18. A method according to Statement 16 or Statement 17, where the aqueous environment is chosen from neutral deionized water, phosphate buffered saline (PBS), cell culture medium, fetal bovine serum (FBS), and the like, and any combination thereof.
Statement 19. A method according to Statement 17 or Statement 18, where, the aqueous environment is comprised within an individual or a portion of an individual (e.g., cells, tissue, blood, plasma, or the like, or any combination thereof).
Statement 20. A method according to any one of Statements 16-19, where the H2S-loaded Zr-MOF(s) is/are taken up by a cell or a population of cells, and where H2S is released within the cell or the population of cells.
Statement 21. A method according to Statement 20, where the cell or the population of cells exhibits greater than about 50% viability (e.g., about 50% or greater, about 60% or greater, about 70% or greater, about 80% or greater, about 90% or greater, or about 100%) after the contacting 20 of the cell or the population of cells with about 1 mg/ml or less of H2S-loaded Zr-MOF(s)).
Statement 22. A method according to Statement 19-21, where the individual is an individual suffering from (or at risk of) an ischemia-reperfusion injury (which may also be referred to as reperfusion injury, reoxygenation injury, hypoxia-ischemia injury, hypoxia-reoxygenation injury, or the like), inflammation (e.g., acute or chronic, local or systemic, or the like), a wound (e.g., an abrasion, a laceration, a puncture, or an avulsion), or the like, or any combination thereof, and where delivery treats or prevents the ischemia-reperfusion injury, the inflammation, the wound, or the like, or any combination thereof, in the individual. In various examples, a desorbed Zr-MOF is used to make a H2S-loaded Zr-MOF of the present disclosure, such as, for example, according to any one of Statement 10-13 or prepared by a method according to Statement 14.
The steps of the methods described in the various embodiments and examples disclosed herein are sufficient carry out the methods of the present disclosure. Thus, in an embodiment, a method consists essentially of a combination of the steps of the methods disclosed herein. In another embodiment, a method consists of such steps.
The following example is presented to illustrate the present disclosure. It is not intended to be limiting in any manner.
This example provides a description of MOFs and methods of the present disclosure.
A strategy for controlled delivery of H2S is to design biocompatible porous solids capable of storing and controllably releasing gaseous H2S, avoiding the formation of biologically-active byproducts. A strategy to identify new MOFs capable of reversibly adsorbing H2S is to leverage its properties as a hydrogen-bond donor and weak hydrogen-bond acceptor, similar to water. In particular, we hypothesized that the surprisingly strong binding of water −ΔHads of approximately 60 kJmol−1) in Zr6O4(OH)4(fumarate)6 or MOF-801 (
Through combined experimental and computational analyses we demonstrated that MOF-801, as well as the related biocompatible mesaconate-based framework Zr-mes and itaconate-based framework CORN-MOF-2 (CORN=Cornell University) undergo strong but reversible adsorption of H2S with minimal framework degradation (
Results and Discussion. Preparation of MOFs. The MOFs Zr6O4(OH)4(fumarate)6 and Zr6O4(OH)4(mesaconate)6 are also known as MOF-801 and Zr-mes, respectively. We refer to these frameworks as Zr-fum and Zr-mes, respectively, for clarity. Following procedures adapted from the literature, we prepared Zr-fum and Zr-mes under solvothermal conditions on 10 mmol scale. Specifically, these frameworks were synthesized from ZrOCl2·8H2O and the corresponding dicarboxylic acid in either N,N-dimethylformamide (Zr-fum-DMF, Zr-mes-DMF) or water (Zr-fum-H2O, Zr-mes-H2O) using formic acid as a modulator. After optimization, 30 equivalents of formic acid were found to produce Zr-fum and Zr-mes with high crystallinity, as determined by powder X-ray diffraction (PXRD). Notably, higher concentrations of formic acid led to the formation of significant impurities. The PXRD patterns of solvated Zr-fum and Zr-mes prepared in DMF and in H2O are shown in
We hypothesized that the key to preparing high-quality Zr-ita was to avoid the use of base during MOF synthesis. Consistently, employing water as the solvent instead of DMF produced semi-crystalline Zr-ita-H2O for the first time (
H2S adsorption in MOFs. After preparing Zr-fum-H2O, Zr-mes-H2O, and Zr-ita-2O, we next evaluated the reversible H2S capture performance of all three frameworks by carrying out isothermal adsorption measurements at 25° C., 40° C., and 55° C. (
The differential enthalpies of adsorption (−ΔHads) for all three frameworks are included in
The reversibility of H2S adsorption and long-term stability towards H2S are also critical criteria for prospective H2S-storage materials. As such, we carefully evaluated the stability of Zr-fum-H2O, Zr-mes-H2, and Zr-ita-H2O towards H2S in both the gas and solution phases. To characterize the stability of Zr-fum-H2O, Zr-mes-H2O, and Zr-ita-H2O to H2S in solution, we soaked each MOF in a 0.8 M solution of H2S in THF at 50° C. for 48 h. Negligible changes in the PXRD patterns, infrared spectra, and 1H-NMR spectra after digestion with a saturated K3PO4/D2O solution were observed for the MOFs after exposure to H2S in solution, suggesting that, in contrast to Zn-MOF-74, little-to-no framework degradation occurred under these conditions.
Consistent with the desorption data in
Due to the microcrystalline nature of the MOFs studied herein, we were unable to study the binding modes of H2S within each MOF by single-crystal X-ray diffraction. Thus, we turned to density functional theory (DFT) calculations to probe the structure of H2S bound within Zr-fum, Zr-mes, and Zr-ita (
H2S delivery from MOFs. Prior to evaluating the ability of H2S-loaded Zr-fum, Zr-mes, and Zr-ita to release H2S under physiologically relevant conditions, we evaluated the stability of these frameworks under aqueous conditions as well as their biocompatibility. Similar to other Zr-MOFs, all three frameworks were found to be stable in neutral deionized water (pH 7.0) and cell culture medium (pH 7.4) prepared from Dulbecco's Modified Eagle's Medium (DMEM) supplemented with 10% fetal bovine serum (FBS) over extended periods (3-10 days). Based on its high H2S capacity and stability under physiological conditions, we selected Zr-fum-H2O as a promising framework to study further for H2S delivery. The biocompatibility of Zr-fum-H2O was assessed by exposing HeLa cells to varying amounts of activated framework suspended in DMEM supplemented with 10% FBS for 72 h at 37° C. (
given the large excess of free DNS-az present in solution, this suggests that the release of H2S from Zr-fum-H2O is complete in less than 30 s. Importantly, a control experiment in which H2S was dosed into a tube lacking MOF and then “poured” into PBS following the same procedure produced no detectable amounts of H2S, confirming that all of the H2S was released from Zr-fum-H2O (black line,
We demonstrated that biocompatible MOFs that are completely stable to H2S, including Zr-fum, Zr-mes, and Zr-ita, present a promising new direction for the design of vehicles for H2S release under physiological conditions. In particular, given its excellent stability, high H2S capacity, lack of toxicity, ambient stability, and performance in a cellular hypoxia-reoxygenation injury assay, Zr-fum-H2O represents a next-generation platform for the therapeutic delivery of H2S. In addition to Zr-fum-H2O, this work also adds Zr-mes-H2O and Zr-ita-H2O to the growing lexicon of biocompatible MOFs for drug delivery applications. Future work will focus on functionalizing the surface of these frameworks to further control the rate and location of H2S delivery under physiological conditions.
General procedures. All reagents were purchased from commercial vendors and used without additional purification. The metal salts zirconyl chloride octahydrate (98%, Alfa Aesar) and zirconium (IV) chloride (99.5%, Alfa Aesar) were kept in desiccators when not in use. Fumaric acid (99%), mesaconic acid (99%), 2,5-dihydroxyterephthalic acid (H4dobdc, 95%), reagent-grade N,Ndimethylformamide (DMF), lead (II) chloride (anhydrous, 99.99%), potassium bromide (99%), sodium azide (99%), zinc nitrate hexahydrate (98%), and sodium sulfide nonahydrate (98%) were purchased from Sigma-Aldrich. Itaconic acid (99%, Alfa Aesar) was provided by the group of Prof. Brett Fors (Cornell University). Reagent-grade acetic acid was purchased from EMD Chemicals. Reagent-grade formic acid was purchased from Mallinckrodt Chemical. Absolute ethanol, acetonitrile, hexanes, methanol, dichloromethane (DCM), tetrahydrofuran (THF, 99%), tripotassium phosphate (99%), pH 3 buffer (potassium hydrogen phthalate), pH 7 buffer (monopotassium phosphate, sodium hydroxide, water), and pH 10 buffer (potassium hydroxide, potassium carbonate, potassium borate, water) solutions were purchased from Fisher Scientific or VWR. 5-(dimethylamino)naphthalene-1-sulfonyl chloride (dansyl chloride, 98%) was purchased from Cayman Chemical. Phosphate buffered saline (PBS) and fetal bovine serum (FBS) were purchased from Corning Life Sciences (Tewksbury, MA). A cylinder of hydrogen sulfide (H2S, 99.5%) was purchased from Airgas. A solution of H2S in THF (0.8 M) was purchased from Fluka Chemical. Deuterated dimethyl sulfoxide (DMSO-d6, 99%) and deuterium oxide (D2O, 99.9%) were purchased from Cambridge Isotope Laboratories. Infrared spectra were collected on a Bruker Tensor II IR spectrometer with a diamond Attenuated Total Reflectance (ATR) attachment. Diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS) spectra were collected on a Bruker Tensor II IR spectrometer with a Harrick Praying Mantis attachment in a low temperature reaction chamber. Fluorescence spectra were measured using a Cary Eclipse fluorescence spectrophotometer (Agilent, Santa Clara, CA). Surface area data were collected on a Micromeritics 3-flex gas sorption analyzer using ultrapure N2 (99.999%) and a liquid N2 bath. Brunauer-Emmett-Teller (BET) and Langmuir surface areas were determined by linear least squares regression analysis using the linearized forms of the BET and Langmuir equations, respectively. Water and H2S adsorption isotherms were collected on a Micromeritics 3-flex gas sorption analyzer. MOFs were activated at 100° C. or 180° C. in the case of Zn-MOF-74 for 48 h prior to any gas sorption measurements. Powder X-ray diffraction (PXRD) patterns were collected on a Rigaku Ultima IV diffractometer equipped with a CuKα source (λ=1.54 Å) and were baseline corrected after data collection. 1H-NMR data were collected on a Bruker INOVA 500 MHz spectrometer and are referenced to residual solvent. The use of this instrument is supported by the National Science Foundation (CHE-1531632). Decomposition profiles were collected on a Q500 V6.7 thermogravimetric analyzer using a temperature ramp of 5.00° C./min from room temperature to 800.00° C. Scanning electron microscopy images were taken at 1.0 kV using a Zeiss Gemini 500 scanning electron microscope. The powder samples were immobilized on carbon tape mounted on an aluminum stub. The samples were blown using compressed air to remove excess material not stuck to the tape and then were coated with a carbon layer. X-ray photoelectron spectroscopy (XPS) spectra were collected using a Scienta Omicron ESCA-2SR with an operating pressure of 1×10-9 Torr. Monochromatic Al Kα x-rays (1486.6 eV) were generated at 300 W (15 kV; 20 mA) with photoelectrons collected from a 2 mm diameter analysis spot. Photoelectrons were collected at a 0° emission angle with a source to analyzer angle of 54.7°. A hemispherical analyzer determined the electron kinetic energy, using a pass energy of 200 eV for wide/survey scans, and 50 eV for high resolution scans. A flood gun was used for charge neutralization on all samples. Survey scans, C1s, O1s, and S2p high resolution scans were collected for all samples. Zn2p and Zr3d high resolution scans were collected for Zn-MOF-74 and Zr-fum samples, respectively. Spectra were analyzed in CasaXPS; each scan was binding energy calibrated to the C1s primary peak position set to 284.8 eV. H2S adsorption data were fit using the Dual-Site Langmuir-Freundlich model (Eq. 2), where Q(P) is the predicted uptake Q at pressure P in mmol/g, Qsati is the saturation pressure of binding site i in mmol/g, bi is the Langmuir parameter of site i, vi is the Freundlich parameter of site i, —Si is the entropy of binding site i in J/mol·K, R is the ideal gas constant, Ei is the enthalpy of adsorption for binding site i in kJ/mol, and T is the temperature in K. The isotherms were fit with either v1 and v2 set as 1 (Dual-Site Langmuir model) or with v1 and v2 allowed to vary freely (Langmuir-Freundlich model). Fits were obtained using Solver in Microsoft Excel.
Heats of adsorption were calculated using the Clausius-Clapeyron equation (Eq. 3), where PQ are pressure values corresponding to the same loading Q, −ΔHads is the differential enthalpy of adsorption in kJ/mol, R is the ideal gas constant, T is the temperature in K, and c is a constant. Fits over a range of Q values were obtained using Mathematica.
Small-scale preparations of MOFs under aqueous conditions with formic acid as modulator. Zr-fum-H2O. Fumaric acid (58.0 mg, 0.50 mmol, 1.00 eq) and ZrOCl2·8H2O (161 mg, 0.50 mmol, 1.00 eq) were added to a 15 mL screw cap reaction tube along with deionized water (2 mL). Next, either 0 eq, 10 eq (189 μL, 5.00 mmol), 30 eq (566 μL, 15.0 mmol), 50 eq (943 μL, 25.0 mmol) or 80 eq (1.51 mL, 40.0 mmol) of formic acid were added. The tube was heated to 95° C. in an aluminum heating block without stirring for 24 h. After removing the tube from the heating block and allowing it to cool to room temperature, the remaining solvent was pipetted off of the settled precipitate and replaced with fresh ethanol (10 mL). The ethanol was replaced once every 24 h for three days. Powder X-ray diffraction patterns were collected after the last ethanol soak.
Zr-mes-H2O. Mesaconic acid (65.0 mg, 0.50 mmol, 1.00 eq) and ZrOCl2·8H2O (161 mg, 0.50 mmol, 1.00 eq) were added to a 15 mL screw cap reaction tube along with deionized water (2 mL). Next, either 0 eq, 30 eq (566 μL, 15.0 mmol), 50 eq (943 μL, 25.0 mmol) or 80 eq (1.51 mL, 40.0 mmol) of formic acid were added. The tube was heated to 95° C. in an aluminum heating block without stirring for 24 h. After removing the tube from the heating block, the remaining solvent was pipetted off of the settled precipitate and replaced with fresh ethanol (10 mL). The ethanol was replaced once every 24 h for three days. Powder X-ray diffraction patterns were collected after the last soak.
Preparation and characterization of Zr6O4(OH)4(fumarate)6, Zr-fum-DMF. This procedure was adapted from the literature. Fumaric acid (1.16 g, 10.0 mmol, 1.00 eq), ZrOCl2·8H2O (3.24 g, 10.0 mmol, 1.00 eq), and formic acid (14.0 mL, 371 mmol, 37.0 eq) were added to a screw cap, high pressure reaction vessel equipped with a stir bar. Next, DMF (40 mL) was added, and the reaction vessel was sealed. The mixture was stirred and heated at 120° C. for 24 h. The heterogeneous reaction mixture was allowed to cool to room temperature and filtered.
The resulting precipitate was transferred into a screw cap jar filled with DMF (80 mL), and the mixture was allowed to stand for 24 h at room temperature. The DMF was then decanted and replaced with the same volume of fresh DMF. This procedure was repeated an additional two times for a total of three DMF soaks, at which point the DMF was replaced with ethanol (80 mL), and the process repeated another three times for a total of six washes. The solid was then activated under high vacuum (<100 mbar) at 100° C. overnight to yield Zr6O4(OH)4(fumarate)6 as a white solid.
Preparation and characterization of aqueous Zr6O4(OH)4(fumarate)6, Zr-fum-H2O. Fumaric acid (1.16 g, 10.0 mmol, 1.00 eq), ZrOCl2·8H2O (3.24 g, 10.0 mmol, 1.00 eq), and formic acid (11.3 mL, 300 mmol, 30.0 eq) were added to a screw cap, high pressure reaction vessel equipped with a stir bar. Next, deionized water (40 mL) was added, and the reaction vessel was sealed. The mixture was stirred and heated at 95° C. for 24 h. The heterogeneous reaction mixture was allowed to cool to room temperature. After cooling, the mixture was transferred into a centrifuge tube and centrifuged at 4000 rpm for 10 minutes two times. The solvent was decanted, and the resulting precipitate was transferred into a screw cap jar filled with ethanol (80 mL). The solid was allowed to stand for 24 h at room temperature. The mixture was centrifuged as detailed above. The ethanol was then decanted and replaced with the same volume of fresh ethanol. This procedure was repeated a total of three times. The solid was then activated under high vacuum (<100 mbar) at 100° C. overnight to yield Zr6O4(OH)4(fumarate)6 as a white 20 solid.
Preparation and characterization of Zr6O4(OH)4(mesaconate)6, Zr-mes-DMF. Mesaconic acid (1.30 g, 10.0 mmol, 1.00 eq), ZrOCl2·8H2O (3.24 g, 10.0 mmol, 1.00 eq), and formic acid (14.0 mL, 371 mmol, 37.0 eq) were added to a screw cap, high pressure reaction vessel equipped with a stir bar. Next, DMF (40 mL) was added, and the reaction vessel was sealed. The mixture was stirred and heated at 120° C. for 24 h. The heterogeneous reaction mixture was allowed to cool to room temperature and filtered. The resulting precipitate was transferred into a screw cap jar filled with DMF (80 mL), and the mixture was allowed to stand for 24 h at room temperature. The DMF was then decanted and replaced with the same volume of fresh DMF. This procedure was repeated an additional two times for a total of three DMF soaks, at which point the DMF was replaced with ethanol (80 mL) and the process repeated another three times for a total of six washes. The solid was then activated under high vacuum (<100 mbar) at 100° C. overnight to yield Zr6O4(OH)4(mesaconate)6 as a fine white powder.
Preparation and characterization of aqueous Zr6O4(OH)4(mesaconate)6, Zr-rmes-H2O. Mesaconic acid (1.30 g, 10.0 mmol, 1.00 eq), ZrOCl2·8H2O (3.24 g, 10.0 mmol, 1.00 eq), and formic acid (11.3 mL, 300 mmol, 30.0 eq) were added to a screw cap, high pressure reaction vessel equipped with a stir bar. Next, deionized water (40 mL) was added, and the reaction vessel was sealed. The mixture was stirred and heated at 95° C. for 24 h. The heterogeneous reaction mixture was allowed to cool to room temperature and filtered. The precipitate was transferred into a screw cap jar filled with ethanol (80 mL), and the mixture was allowed to stand for 24 h at room temperature. The ethanol was then decanted and replaced with the same volume of fresh ethanol. This procedure was repeated a total of three times. The solid was then activated under high vacuum (<100 mbar) at 100° C. overnight to yield Zr6O4(OH)4(mesaconate)6 as a fine white powder.
Preparation and characterization of Zr6O4(OH)4(itaconate)6, Zr-ita-DMF. Various acid modulators including acetic acid, L-proline, HC1, pivalic acid, and formic acid were used in an attempt to produce crystalline Zr-ita-DMF. However, in all cases amorphous solids were produced (not shown). Thus, a large-scale batch was prepared with no acid modulator for further characterization. Itaconic acid (0.98 g, 7.50 mmol, 1.00 eq) and ZrCl4 (1.75 g, 7.50 mmol, 1.00 eq) were added to a screw cap, high pressure reaction vessel equipped with a stir bar. Next, DMF (150 mL) and deionized water (0.40 mL, 22.5 mmol, 3.00 eq) were added, and the reaction vessel was sealed. The mixture was stirred and heated at 120° C. for 24 h. The heterogeneous reaction mixture was allowed to cool to room temperature and filtered. The precipitate was transferred into a screw cap jar filled with DMF (80 mL), and the mixture was allowed to stand for 24 h at room temperature. The DMF was then decanted and replaced with the same volume of fresh DMF. This procedure was repeated an additional two times for a total of three DMF soaks, at which point the DMF was replaced with THF (80 mL) and the process repeated another three times for a total of six washes. The solid was then activated under high vacuum (<100 mbar) at 100° C. overnight to yield Zr6O4(OH)4(itaconate)6 as a white solid.
Characterization of MOFs prepared under aqueous conditions exposed to H2S solution. General procedure. In a nitrogen-filled glovebox, a 15 mL screw cap reaction tube was loaded with desolvated MOF (˜50 mg) and capped. The tube was removed from the glovebox and placed under a dry atmosphere of nitrogen. Next, H2S in THF (0.8 M, 1.0 mL) was added via syringe under a constant stream of nitrogen. The cap was replaced with one that had not been punctured, and the tube was left to stand for 48 h at 50° C. The MOFs were collected by filtration and washed with THF into a filter flask containing bleach to quench any remaining H2S. The solids were then characterized.
Delivery of H2S under biologically relevant conditions. Serum and DI water stabilities. A 5 mL scintillation vial was loaded with desolvated MOF (˜50 mg) and either serum or DI water (3.0 mL) was added via syringe. The vial was capped, and the tube was left to stand for either 3 days (serum) or 10 days (DI water) at room temperature. The serum measurements were carried out using at Dulbecco's Modified Eagle's Medium (DMEM) supplemented with 10% fetal bovine serum (FBS), which is the standard medium used for all cell culture experiments in this work. The MOFs were collected by filtration and washed with deionized water. The solids were then characterized. Together, these results suggest that the MOFs would likely undergo slow degradation upon submersion in serum for extended periods of time, but they are stable enough for delivery of H2S.
Synthesis of 1,5-dansyl azide (DNS-az). This compound was synthesized by a modified literature procedure. A solution of dansyl chloride (250 mg, 0.93 mmol) in ethanol (15 mL) was added dropwise to a rapidly stirred solution of sodium azide (100 mg, 1.54 mmol) in 50% aqueous ethanol (7 mL). The resulting yellow solution was stirred for 4 h, at which time the solvent was removed by rotary evaporation to yield the crude product as a yellow oil. The oil was purified by silica gel chromatography (2:1 hexanes/CH2l2). The pure fractions were pooled and evaporated to yield DNS-az as a bright yellow oil, which was dried under high vacuum overnight. Yield: 190 mg (73.9%). 41 NMR (500 MHz, DMSO-d6): 67 5 8.66 (d, J=10 Hz, 1H), 8.37 (d, J=10 Hz, 1H), 8.03 (d, J=10 Hz, 1H), 7.74 (m, 2H), 7.34 (d, J=10 Hz, 1H), 2.85 (s, 6H). 13C NMR (125 MHz, DMSO-d6): δ 151.97, 132.72, 130.30, 129.60, 129.17, 128.72, 123.75, 117.62, 115.92, 45.06. These spectra are consistent with those reported in the literature.
H2S detection via fluorescence spectroscopy. The turn-on fluorescent probe 1,5-dansyl azide (DNS-az) was used to detect H2S in solution. A known amount of desolvated Zr-ita-H2O or Zr-fum-H2O (50-100 mg) was weighed and activated for 48 h at 100 ° C. under vacuum 30 (<10 μbar). The MOF was then dosed with ˜1 bar of H2S at 30° C. and allowed to equilibrate until <0.01% change in the H2S pressure occurred over a 45 s interval (approximately 3-4 h in each case). The exact amount of H2S adsorbed was recorded. At the time of the experiment, the tube with MOF was purged with N2 for 90 s to remove gaseous H2S before the sample was poured into a stirred solution of phosphate buffered saline (PBS; pH 7.4) at a typical concentration of ˜1 mg MOF/mL of PBS. Assuming a capacity of 4 mmol/g of H2S in Zr-fum-H2O, this corresponds to a maximum concentration of 4 mM for H2S in the PBS solution, if all of the H2S was released by the MOF into solution. A control experiment in which a tube lacking MOF was dosed with H2S, purged with N2 for 90 s, and then “poured” into PBS yielded no detectable amounts of H2S in solution, confirming that this purging procedure is sufficient to remove gaseous H2S from the tube. At 30 second intervals, 300 μL aliquots of the suspension (corresponding to a maximum amount of 1.2 μmol of H2S) was removed (taking care not to remove any solids; a syringe filter was used in the case of Zr-fum-H2) and added to a freshly-prepared solution of DNS-az (25 μmol) in CH3CN (1 mL, final concentration of 25 mM). The large excess of DNS-az (25 μmol) compared to H2S (maximum of 1.2 μmol for Zr-fum-H2O) in the aliquot guarantees that the DNS-az probe should not be saturated during the experiment. The solution was allowed to incubate at 23° C. for 5 min (min=minute(s)) before the fluorescence of the probe was measured at 520 nm (with excitation at 340 nm). Due to unavoidable loss of gaseous H2S to air, this assay cannot be used to reliably quantify the amount of H2S released into solution. However, the kinetics of H2S release were found to be relatively reproducible between samples.
Cell lines and culture conditions. HeLa and H9c2 cells were obtained from American Type Culture Collection (ATCC, Washington D.C.) and cultured as adherent monolayers in a humidified 5% CO2 atmosphere at 37° C. in DMEM supplemented with 10% FBS. Cells were checked for contamination monthly using the PlasmoTest mycoplasma detection kit from InvivoGen (San Diego, CA). Cytotoxicity assay. HeLa or H9c2 cells were seeded in 96-well plates with 2000 cells/well and allowed to reattach overnight. The following day, the culture media was removed, and cells were treated with suspensions containing varying concentrations of the desired MOF in in DMEM supplemented with 10% FBS and incubated for 72 h at 37° C. Following treatment, the cells were incubated in DMEM containing 1 mg/mL (4,5-dimethylthiazol-2-yl)-2,5-diephenyltetrazolium bromide (MTT) without FBS for 3 hours. Following incubation, the media was removed, and the purple formazan crystals were solubilized using 150 μL of an 8/1 S65 DMSO/glyceine buffer (pH 10) mixture. The absorbance at 570 nm of each well was measured using a BioTek Synergy HT plate reader. Results are reported as the average cell viability of 6 wells/concentration compared to untreated cells from three independent trials, with the standard deviation (SD) reported as the error (±SD).
Cellular hypoxia-reoxygenation model of ischemia-reperfusion injury. On the day before the experiment, H9c2 rat cardiomyoblast cells were seeded in a 96 well plate at a density of 8000 cells/well and incubated at 37° C. overnight. To initiate the experiment, the culture media was removed, and the cells were washed with 100 μL of PBS. The assay was initiated by placing the cells in 200 μL of modified Gey's balanced salt solution (GBSS) containing 120 mM NaCl, 5 mM KCl, 1.5 mM CaCl2, 0.28 mM MgSO4, 1 mM MgCl2, 0.840 mM Na2HPO4, 0.220 mM KH2PO4, and 27 mM NaHCO3. The plates were then placed in a hypoxia chamber and flushed with 5% CO2 in N2 for 10 minutes. The chamber was sealed, and the cells were incubated under hypoxic conditions for 2.5 h at 37° C. Following hypoxia, the cells were incubated under normoxic conditions in DMEM containing 10% FBS and the H2S-loaded Zr-fum-H2O at a concentration of 0.05 mg/mL for 24 h prior to measuring the viability using the MTT assay as described above. Viability is reported relative to control cells that were incubated under normal culture conditions throughout the experiment. Another set of control cells were incubated with the MOF without previous incubation under hypoxic conditions. Results are reported as the average viability from 12 wells of a 96 well plate from three independent trials, with the standard deviation (SD) reported as the error (±SD) (ns=not significant, ***p<0.005).
H2S Imaging in HeLa cells with WSPS. Approximately 1×105 HeLa cells were seeded in 35 mm glass-bottomed dishes (MatTek Life Sciences, Ashland, MA) and incubated overnight at 37° C. The following day, the media was removed and the cells were treated with DMEM without FBS containing 1 mM cetyl trimethyl ammonium bromide (CTAB) and 15 μM WSPS (Cayman Chemicals, Ann Arbor, MI; WSP=Washington State Probe) and incubated for 30 min at 37° C. in the dark. The dye-containing media was removed, and the cell layer was washed with PBS (2×1 mL) before treatment with either 0.05 mg/mL of H2S-loaded Zr-fum-H2O or 200 μM Na2S in DMEM without FBS. The cells were then incubated for 1 h at 37 ° C. At the time of imaging, the media was removed, and the cells were washed with 1 mL PBS. Fluorescence images were collected in PBS using a Zeiss LSM710 confocal fluorescence microscope fitted with a 10×water objective with an excitation wavelength of 514 nm and an emission window of 535-657 nm. Images were analyzed and quantified using ImageJ (NIH) and the corrected total cellular fluorescence (CTCF) was calculated using the following formula: CTCF=Integrated density−(area of cell×mean fluorescence of the background) The average of 8 individual cells was used to determine the average CTCF for each replicate. Results are reported as the average of three biological replicates. Qualitative monitoring of H2S release via lead test strips. The formation of lead sulfide on lead chloride-soaked filter paper was used to visually confirm H2S release from Zr-mes-H2O, Zr-fum-H2, and Zr-ita-H2O under ambient conditions. Filter paper cut into thin strips was dipped into a 1 wt % aqueous lead (II) chloride solution and dried for ten minutes. Once dried, the strips were added to a 25 mL scintillation vial containing ˜100 mg of H2S-loaded MOF prepared under the same conditions as described above. Black or orange lead sulfide precipitation on the strips resulted immediately upon contact with the MOF and/or vial glass. The vials were capped, and the old strips removed and replaced once per day until they no longer turned black or orange. Images were taken of the vials each day. As a control, the same assay was used to monitor the release of H2Sfrom a similar amount of Na2S·9H2O and NaSH. Owing to the rapid hydrolysis of both salts (complete degradation/dissolution within 5 h). the lead strip was not changed through the duration of the assay
Computational and structural details. To elucidate the H2O and H2S adsorption mechanisms, we performed first-principles density functional theory (DFT) calculations using a plane-wave basis and projector augmented-wave (PAW) pseudopotentials with the Vienna ab-initio Simulation Package (VASP) code. To include the effect of the van der Waals (vdW) dispersive interactions on binding energies, we performed structural relaxations with Grimme's D3 correction as implemented in VASP. For all calculations, we used (i) a Γ-point sampling of the Brillouin zone and (ii) a 600 eV plane-wave cutoff energy. We explicitly treated twelve valence electrons for Zr (4s24p64d25s2), six for S (3s23p4), six for O (2s22p4), four for C (2s22p2), and one for H (1s1). All structural relaxations were performed with a Gaussian smearing of 0.05 eV. The ions were relaxed until the Hellmann-Feynman forces were less than 0.01 eVA−1. Using above input parameters, we relaxed both internal coordinates and volumes. To compute the H2O and H2S binding energies, we optimized MOFs prior to H2O and H2S adsorptions (EMOF), interacting with 2O and H2S in the gas phase (EH2O|H2S) within a 20 Å×20 Å×20 Å cubic supercell, and MOF with adsorbed H2O and H2S molecules (EH2O|H2S-MOF) using a rigid MOF. The binding energies (EB) were obtained via the difference EB=EH2O|H2S-MOF−(EMOF+EH2O|H2S). The idealized Zr6O4(OH)4(RCO2)6 clusters of Zr-fum, Zr-mes, and Zr-ita contain a mixture of four OH— and four O2-sites to achieve charge neutrality. Initially, we computationally generated these structures without explicitly treating the protons on the Zr6O8 clusters for simplicity. The calculated structure of Zr-fum shows excellent agreement with the previously reported single-crystal X-ray diffraction structure of MOF-801.
H2S and aqueous stability studies with Zn-MOF-74. Preparation of Zn-MOF-74. This procedure is adapted from the literature. A 350 mL, screw-cap high pressure reaction vessel equipped with a stir bar was charged with Zn(NO3)2·6H2O (2.23 g, 7.50 mmol, 3.00 eq.), H4dobdc (495 mg, 2.50 mmol, 1.00 eq.), fresh DMF (125 mL), and ethanol (125 mL). The mixture was sonicated until all of the solids dissolved. The reaction mixture was vigorously sparged with N2 for 1 h. The reaction vessel was sealed, and the reaction mixture was allowed to stir slowly at 120° C. for 14 h, resulting in precipitation of a yellow powder from solution. The reaction mixture was cooled to room temperature and filtered. The collected solid was quickly transferred to a 500 mL Pyrex jar filled with DMF (250 mL). The jar was placed in an oven that had been pre-heated to 120° C. and left to stand for 24 h, after which time the nonhomogeneous mixture was filtered. The collected solid was returned to the jar with fresh DMF (250 mL and returned to an oven that had been pre-heated to 120° C. This soaking process was repeated two more times. The mixture was then filtered and transferred to a 500 mL Pyrex jar filled with methanol (250 mL), and the jar was placed in an oven that had been pre-heated to 60° C. and left to stand 24 h, after which time the non-homogeneous mixture was filtered. The collected solid was returned to the jar with fresh methanol (250 mL) and returned to an oven that had been pre-heated to 60° C. This soaking process was repeated two more times. The mixture was filtered a final time, and the collected solid was quickly transferred to a Schlenk flask under N2. The material was activated under flowing N2 at 180° C. for 24 h, and then by heating under high vacuum at 180° C. for 24 h.
DRIFTS measurements. To measure the DRIFTS spectrum of free H2S gas, the sample cup of the Harrick low temperature reaction chamber was filled with KBr and evacuated to <10 mTorr before dosing with H2S (400 mbar). To measure the DRIFTS spectrum of Zr-fum-H2O and H2S-dosed Zr-fum-H2O, the sample cup of the Harrick low temperature reaction chamber was filled with a 1:5 mixture of Zr-fum-H2O and KBr. The mixture was then activated at 100° C. for 18 hours using a Harrick ATK-024-3 temperature controller under high vacuum (<10 mTorr). The reaction chamber was subsequently pulsed with H2S until desired pressures of 500, 750 and 1000 mbar were reached before immediately closing the chamber and measuring IR spectra.
Although the present disclosure has been described with respect to one or more particular embodiments and/or examples, it will be understood that other embodiments and/or examples of the present disclosure may be made without departing from the scope of the present disclosure.
This application claims the benefit of U.S. Provisional Patent Application No. 63/325,289, filed Mar. 30, 2022; the contents of the above-identified applications are hereby fully incorporated herein by reference in their entirety.
This invention was made with government support under grant number GM138165 awarded by the National Institutes of Health. The government has certain rights in the invention.
| Number | Date | Country | |
|---|---|---|---|
| 63325289 | Mar 2022 | US |
