Method of forming phase change material
11555137 · 2023-01-17
Assignee
Inventors
Cpc classification
B01J20/226
PERFORMING OPERATIONS; TRANSPORTING
Y02E60/14
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B29C33/3807
PERFORMING OPERATIONS; TRANSPORTING
C01B37/00
CHEMISTRY; METALLURGY
C07F7/00
CHEMISTRY; METALLURGY
C08G83/001
CHEMISTRY; METALLURGY
C09K5/08
CHEMISTRY; METALLURGY
International classification
C09K5/06
CHEMISTRY; METALLURGY
Abstract
A method to form a phase change material (PCM). The method includes preparing a polymer solution by mixing an amount of a polymer in a solvent and mixing the polymer solution with an UiO-66 metal-organic framework (MOF) to form a composite. The polymer is a polyethylene glycol (PEG). The method further includes subjecting the composite to ultrasonic agitation and evaporating the solvent from the composite to form the PCM. After the evaporation of the solvent, particles of the PCM exhibit rounded octahedral structures.
Claims
1. A method to form a phase change material (PCM), comprising: preparing a polymer solution by mixing an amount of a polymer in a solvent, wherein the polymer is a polyethylene glycol (PEG); mixing the polymer solution with an UiO-66 metal-organic framework (MOF) to form a composite; subjecting the composite to ultrasonic agitation; and evaporating the solvent from the composite to form the PCM;, wherein a weight ratio of PEG:UiO-66 MOF in the PCM is 0.5:0.2 to 1.0:0.2, wherein the PCM has first particles and second particles, wherein the first particles comprise PEG and the UiO-66 MOF and are smaller than the second particles, wherein the second particles comprise only the UiO-66 MOF and have a longest dimension of 200 nm to 500 nm, wherein the first particles and second particles have a rounded octahedral shape, and wherein the second particles are connected through a network of the first particles.
2. The method of claim 1, wherein, the solvent is ethanol; the PEG has an average molecular weight of from 4000 to 10000.
3. The method of claim 2, wherein the PEG for preparing the polymer solution has an average molecular weight of 6000.
4. The method of claim 1, wherein the PCM has a thermal conductivity of from 0.8 to 0.9 W/mK; and the PCM has an energy storage efficiency of from 92% to 97%.
5. The method of claim 1, wherein the ss-PCM has a latent heat value of from 125 J/g to 175 J/g at a PEG:UiO-66 weight ratio of 0.5, and the ss-PCM has a thermal conductivity of from 0.4 W/mK to 0.6 W/mK at a PEG: UiO-66 weight ratio of 0.5.
6. The method of claim 1, wherein the mixing the polymer solution further comprises mixing carbon nanotubes (CNTs) with at least one of the polymer solution, the MOF, or a combination of both the polymer solution and the MOF to form a PCM containing carbon nanotubes.
7. The method of claim 6, wherein the PCM comprises the CNTs in an amount of from 1 wt % to 4 wt % of the PCM.
8. The method of claim 1, wherein the PCM has an impregnation ratio of at least 60%.
9. The method of claim 1, wherein the PCM has: a freezing temperature of at least 35° C.; and a melting temperature of at least 55° C.
10. The method of claim 1, wherein the PCM has an impregnation efficiency of at least 55%.
11. The method of claim 1, wherein the PCM has a heat storage efficiency of at least 99%.
12. The method of claim 1, wherein the PCM has an energy storage ability of at least 70%.
13. The method of claim 1, wherein the PCM has a latent heat in a freezing process of at least 100 J/g.
14. The method of claim 1, wherein the PCM has a latent heat in a melting process of at least 110 J/g.
15. The method of claim 1, wherein the mixing the polymer solution further comprises including an amine group-containing compound with at least one of the polymer solution, the MOF, or a combination of both the polymer solution and the MOF.
16. The method of claim 1, wherein the weight ratio of PEG to UiO-66 is 0.5:0.2.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1) A more complete appreciation of this disclosure and many of the attendant advantages thereof will be readily obtained as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings, wherein:
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DETAILED DESCRIPTION
(25) The definitions of the terms as used herein are as follows. Unless specified otherwise, these terms are used alone or in combination with another term in the meaning as defined.
(26) Throughout the specification and the appended claims, a given chemical formula or name shall encompass all isomers (stereo and optical isomers and racemates) thereof where such isomers exist. Unless otherwise indicated, all chiral (enantiomeric and diastereomeric) and racemic forms are within the scope of the disclosure. Many geometric isomers of C═C double bonds, C═N double bonds, ring systems, and the like can also be present in the compounds, and all such stable isomers are contemplated in the present disclosure. Cis- and trans- (or E- and Z-) geometric isomers of the compounds of the present disclosure are described and may be isolated as a mixture of isomers or as separated isomeric forms.
(27) All processes used to prepare compounds of the present disclosure and intermediates made therein are considered to be part of the present disclosure. Both the free form and salts of products are within the scope of the disclosure. If so desired, one form of a compound may be converted into another form. Further, a given chemical formula or name shall encompass all conformers, rotamers, or conformational isomers thereof where such isomers exist. Different conformations can have different energies, can usually interconvert, and are very rarely isolatable.
(28) The term “latent heat” as used herein, refers to the energy absorbed or released by a substance during a change in its physical state, wherein said change occurs without a corresponding change in its temperature. One or more substances having high latent heat may be used for energy storage which include acetic acid, acetone, alcohol (ethyl or methyl), aluminum, ammonia, aniline, benzene, bismuth, brass, carbon dioxide, carbon tetrachloride, cast iron, chromium, cobalt, copper, decane, dodecane, ethyl ether, ethylene glycol, glycerin, heptane, hexane, iron, manganese, naphthalene, nickel, octane, paraffin, phenol, platinum, silver, water, and zinc.
(29) The term “PCM” or “Phase Change Material” as used herein, refers to those substances which can absorb or release a large amount of latent heat, as defined herein, when they go through a change in their physical state, i.e., from one physical state to other physical state and vice-versa. Non-limiting examples of PCMs include paraffin-based materials, acids, sugars, sulfates, chlorides, aluminum, copper, gold, iron, lead, lithium, silver, titanium, zinc, nitrates, hydroxides, fatty acids, alcohols, and glycols.
(30) The term “ss-PCM” or “Shape Stabilized PCM” as used herein, refers to PCMs, as defined herein, which use porous matrices as support. Non-limiting examples of porous support matrices include mesoporous carbon, mesoporous silica, graphene, carbon nanotubes, metal foams, and metal-organic frameworks.
(31) As used herein “metal-organic frameworks” or MOFs are compounds having a lattice structure made from (i) a cluster of metal ions as vertices (“cornerstones”)(“secondary building units” or SBUs) which are metal-based inorganic groups, for example metal oxides and/or hydroxides, linked together by (ii) organic linkers. The linkers are usually at least bidentate ligands which coordinate to the metal-based inorganic groups via functional groups such as carboxylates and/or amines. MOFs are considered coordination polymers made up of (i) the metal ion clusters and (ii) linker building blocks. Preferably a UiO-66 MOF is deployed according to certain embodiments of the present disclosure. The UiO-66 MOF is made up of [Zr.sub.6O.sub.4(OH).sub.4] clusters with 1,4-benzodicarboxylic acid struts. The terephthalic acid can be substituted with one or more alkyl groups, one or more carboxylic acids, or one or more phosphate groups. Non-limiting examples of suitable MOFs include UiO66-NH2, UiO-67, UiO-68, HKUST-1, LIC-1, CPL-2, Cu-MOF, Cu-TDPAT, Ni-MOF, Zr-MOF, Zn-TSA Fe—P-MOF, TMU-16-NH2 F-MOF-1, MOP-1, MOF-74, MOF-101, MOF-177, MOF-235, MOF-253, MOF-5, IRMOF-16, MIL-53, MIL-53(Al)—NH.sub.2, MIL-88A, MIL-88-Fe, MIL-88B-4CH3, MIL-100-Fe, MIL-101, PCN-333-Al, ZIF-8, ZIF-67, and ZIF-90.
(32) The term “PEG” or “Polyethylene glycol” as used herein, refers to a condensation polymer of ethylene oxide and water, preferably synthesized using a ring-opening polymerization of ethylene oxide to produce a range of molecular weights and molecular weight distributions. PEGs can be synthesized in linear, branched, Y-shaped, star, comb, or multi-arm geometries. Non-limiting examples of PEG include PEG-100, PEG-200, PEG-400, PEG-600, PEG-800, PEG-1000, PEG-2000, PEG-4000, PEG-6000, PEG-8000,PEG-10000.
(33) The term “PolyMOF” or “Polymer-MOF” as used herein, refers to MOFs synthesized using organic polymers as the organic component of the MOF lattice. One or more polymers may be used in the polymer solution such as alkylene glycol, e.g., ethylene glycol and/or propylene glycol, polyvinylpyrrolidone, or poly (N-(2-hydroxypropyl) methacrylamide) (PHPMA). Non-limiting examples of organic polymers include epoxies, phenolics, polyurethanes, polyimides, amino resins, bismaleimides, glycidyls, aliphatic amines, cycloaliphatic amines, polyaminoamides, anhydrides, isocyanates, and polylactides.
(34) The term “PEG-MOF” as used herein, refers to polyMOFs, as defined herein, in which the polymer used as the organic component of the MOF lattice is a PEG organic polymer.
(35) In the drawings, like reference numerals designate identical or corresponding parts throughout the several views. As used herein, the words “a,” “an” and the like generally carry a meaning of “one or more,” unless stated otherwise. Further, the terms “approximately,” “approximate,” “about,” and similar terms generally refer to ranges that include the identified value within a margin of 25%, 20%, 10%, or 5%, and any values therebetween. Furthermore, the terms “equal to,” “substantially equal to,” and similar terms generally refer to ranges that include the identified value within a margin of 75%, 80%, 85%, 90%, 95%, or 100%, and any values therebetween.
(36) As used herein, the terms “optional” or “optionally” means that the subsequently described event(s) can or cannot occur or the subsequently described component(s) may or may not be present (e.g., 0 wt. %).
(37) Aspects of the present disclosure are directed to a method to form a phase change material (PCM) comprising a combination of at least one polymer and at least one MOF. Aspects of the present disclosure are also directed to a method to form a phase change material (PCM) comprising a combination of at least one polymer, at least one MOF, and carbon nanotubes (CNTs). In some examples, the aspects of present disclosure are directed to preparation of composite PCMs comprising at least one organic or inorganic phase change material, at least one MOF, and optionally CNTs. The organic phase change material that may be utilized in various aspects is preferably an organic polymeric material. The inorganic phase change material that may be utilized in various aspects is preferably a hydrated salt or a metallic material. Further aspects of the present disclosure are related to a polymer-MOF based PCM prepared by the methods disclosed herein.
(38) In an aspect of the present disclosure, the method of preparation of a phase change material (PCM) includes preparation of a polymer solution by mixing an amount of a polymer in a solvent; mixing the polymer solution with a metal-organic framework (MOF) to form a composite; subjecting the composite to agitation; and removing the solvent from the composite to form the phase change material (PCM).
(39) The polymer solution may be prepared by mixing a suitable polymer with any compatible solvent. The polymer may be a paraffin- or a non-paraffin-based material. In a non-limiting example, the paraffin-based material may be a paraffin n-carbons material, wherein n represents number of carbon atoms present in the paraffin material and may be greater than or equal to 14 and less than or equal to 34, preferably greater than or equal to 19 and less than or equal to 29, or preferably 24. In another non-limiting example, the non-paraffin-based material may be selected from a group consisting of fatty acids, alcohols, and glycols. In a non-limiting example, the non-paraffin-based material is a fatty acid. In some examples, the fatty acid is caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, or the like. In another non-limiting example, the non-paraffin-based material is an alcohol. In some examples, the alcohol is capric alcohol, lauryl alcohol, myristyl alcohol, cetyl alcohol, stearyl alcohol, or the like. In another preferred embodiment the non-paraffin-based material is a glycol and/or a polyglycol. In some examples, the glycol is a polyethylene glycol (PEG). PEG may be selected from a group of PEG homopolymers within a defined weight average molecular weight range such as for example PEG-200, PEG-400, PEG-600, PEG-800, PEG-1000, PEG-2000, PEG-4000, PEG-6000, PEG-8000, PEG-10000, and the like. In certain embodiments, the PEG may be combined with another polymer such as polyvinyl alcohol, poly (lactic-co-glycolic acid), poly(lactic-co-glycol), polylactic acid, polycaprolactone, polyglycolic acid, polybutylene terephthalate, or polyethylene terephthalate.
(40) The solvent utilized for preparing the polymer solution may be selected based on the choice of the polymer. In a non-limiting example, the solvent may be a polar protic, a polar aprotic, or a non-polar solvent. Exemplary polar protic solvents that may be used include water, methanol, ethanol, isopropyl alcohol, acetic acid, etc. Exemplary polar aprotic solvents that may be used include dichloromethane, tetrahydrofuran, ethyl acetate, acetonitrile, dimethyl formamide, dimethyl sulfoxide, acetone, hexamethylphosphoric triamide, etc. Exemplary non-polar solvents that may be used include pentane, hexane, benzene, carbon tetrachloride, diethyl ether, xylene, toluene, acetic acid, chloroform, and ethyl acetate.
(41) The MOF used in the method of the present disclosure is desired to exhibit at least one of the following characteristics: (a) large surface area, (b) high pore volume, (c) high storage capacity, (d) minimum mass transfer limitation, and (e) high stability especially hydrothermal stability. In an aspect of the present disclosure, the MOF is desired to exhibit characteristic (e) and at least one characteristic selected from (a) to (d). In another aspect of the present disclosure, the MOF exhibits all the aforementioned characteristics. In a preferred embodiment, the particles of the rounded octahedral structure may have a BET surface area from 750 m.sup.2/g to 1250 m.sup.2/g, a micropore volume from 0.25 cm.sup.3/g to 2.5 cm.sup.3/g, and an energy storage efficiency of at least 99%.
(42) Exemplary MOFs suitable for use with the methods of the present disclosure include Zr-based MOFs like UiO-66, UiO-67, MOF-808, NU-1000, Al-based MOFs like MIL-96, MIL-100, MIL-110, Cu-based MOFs like HKUST-1, Cr-based MOFs, Cd-based MOFs, etc. Further, the MOF employed may carry post-synthetic modifications (PSMs), enhancing its desired properties or functionalities. In a non-limiting example, the MOF may have been modified by (a) metal or organic ligand substitution strategy to obtain an MOF with mixed metal/ligands; or (b) chemical function decoration to obtain an MOF decorated and/or substituted with a functional group, for example, but not limited to, an alkyl substituted-, aryl substituted-, an amine decorated-, a carboxylate decorated-, a nitro decorated, or a bifunctional modified-MOF.
(43) In an aspect of the present disclosure, the mixing further comprises mixing carbon nanotubes (CNTs) with at least one of the polymer solution, the MOF, or a combination of both the polymer solution and the MOF. In another aspect of the present disclosure, the mixing further comprises using an amine group-containing compound with at least one of the polymer solution, the MOF, or a combination of both the polymer solution and the MOF. In another aspect of the present disclosure, the mixing further comprises using CNTs and an amine group-containing compound with at least one of the polymer solution, the MOF, or a combination of both the polymer solution and the MOF.
(44) The composite obtained from mixing an MOF and a polymer, according to various aspects of the present disclosure, is further subjected to agitation. The agitation may be performed by any suitable methods known for example, but not limited to, mechanical, magnetic, or ultrasonic. Ultrasonication may be of any suitable power ranging from 20 W to 100 W, preferably 30 W to 90 W, preferably 40 W to 80 W, preferably 50 W to 70 W, or 60 W. Ultrasonication may also be of any suitable time ranging from 10 minutes to 1 hour, preferably 20 minutes to 40 minutes, or 30 minutes.
(45) Further, the composite obtained after the mixing or agitation, is processed to remove or separate the solvent to isolate the phase change material (PCM). In a non-limiting example, the solvent may be removed or separated using decanting, filtration, evaporation, vacuum drying, vacuum evaporation, vacuum concentration, heating, or a combination thereof.
(46) Now turning to a particular aspect of the present disclosure, a method to form a PEG-UiO-66 based PCM is disclosed. The method includes preparation of a PEG polymer solution by mixing an amount of PEG polymer in a solvent; mixing the polymer solution with UiO-66 MOF to form a composite; subjecting the composite to ultrasonic agitation; and evaporating the solvent from the composite to form the PCM.
(47) In another aspect of the present disclosure, a method to form a PEG-UiO-66-CNT based PCM is disclosed. The method includes preparation of a PEG polymer solution by mixing an amount of PEG polymer in a solvent; mixing the polymer solution with an UiO-66 metal-organic framework (MOF) to form a composite; subjecting the composite to ultrasonic agitation; and evaporating the solvent from the composite to form the PCM. Carbon nanotubes (CNTs) are mixed with the solvent and polymer when forming the PEG polymer solution. In other embodiments the carbon nanotubes are mixed with at least one of the polymer solution, the MOF, or a combination of both the polymer solution and the MOF. The formed PCM may comprise CNTs in an amount from 1 wt. % to 4 wt. % of the PCM, preferably at 1.5 wt. % to 3.5 wt. % of the PCM. Preferably 2 wt. % to 3 wt. % of the PCM, or 2.5 wt. % of the PCM.
(48) The solvent employed for preparing the PEG polymer solution in any of the aforementioned aspects may be chosen from any of the above-mentioned exemplary solvent types. In some examples, the solvent is a polar protic solvent. In some examples, the solvent used is ethanol.
(49) Further, the PEG polymer used for preparing the polymer solution, as described in earlier aspects of the present disclosure, may be of any suitable average molecular weight ranging from as low as 200 to as high as 20,000. In some examples, the PEG has an average molecular weight ranging from 2,000 to 10,000. In some examples, the PEG has an average molecular weight ranging from 4,000 to 8,000. In some examples, the PEG has an average molecular weight of about 6,000.
(50) The particles of the PCM obtained by the methods of the present disclosure exhibit rounded octahedral structures. As depicted in
(51) In some aspects, the PCM obtained by the methods of the present disclosure is a shape stabilized phase change material (ss-PCM). The ss-PCM may have a PEG to UiO-66 weight ratio ranging from 1:0.2 to 0.2:1, preferably 0.8:0.4 to 0.4:0.8, or 1:1. In a non-limiting example, the PEG to UiO-66 weight ratio may be such that the PEG is at least 5 times, at least 4.5 times, at least 4 times, at least 3.5 times, at least 3 times, at least 2.5 times, at least 2 times, or at least 1.5 times the UiO-66. In another non-limiting example, the PEG to UiO-66 weight ratio may be such that the UiO-66 is at least 5 times, at least 4.5 times, at least 4 times, at least 3.5 times, at least 3 times, at least 2.5 times, at least 2 times, or at least 1.5 times the PEG.
(52) In some examples, the ss-PCM may have a PEG to UiO-66 weight ratio ranging from 0.5:0.2 to 1:0.2., preferably 0.4:0.3 to 0.75:0.25, or 1:1. In some examples, the PEG to UiO-66 weight ratio may be 0.5:0.2, preferably 0.45:0.25, preferably 0.4:0.3, or 1:1. In some examples, the PEG to UiO-66 weight ratio may be 0.7:0.2, preferably 0.65:0.25, preferably 0.6:0.3, preferably 0.55:0.35, preferably 0.5:0.4, or 1:1. In some examples, the PEG to UiO-66 weight ratio may be 1:0.2, preferably 0.9:0.3, preferably 0.8:0.4, preferably 0.7:0.5, or 1:1. In some examples, the PEG to UiO-66 weight ratio may be 0.5:1, preferably 0.6:0.9, preferably 0.7:0.8. or 1:1. In some examples, the PEG to UiO-66 weight ratio may be 1:1.
(53) The PCM may have a thermal conductivity ranging from 0.8 W/mK to 0.9 W/mK, preferably 0.81 W/mK to 0.89 W/mK, preferably 0.82 W/mK to 0.88 W/mK, preferably 0.83
(54) W/mK to 0.87 W/mK, preferably 0.84 W/mK to 0.86 W/mK, or 0.85 W/mK. In a non-limiting example, the PCM may have a thermal conductivity ranging from 0.4 W/mK to 0.6 W/mK at a PEG to UiO-66 weight ratio of 0.5, preferably 0.42 W/mK to 0.58 W/mK, preferably 0.44 W/mK to 0.56 W/mK, preferably 0.46 W/mK to 0.54 W/mK, preferably 0.48 W/mK to 0.52 W/mK, or 0.5 W/mK.
(55) Further, the PCM may have an energy storage efficiency of at least 99%, preferably at least 98%, 97%, 96%, 95%, 94%, 93%, 92%, 91%, or 90% and heat storage efficiency of at least 99%, preferably at least 98%, 97%, 96%, 95%, 94%, 93%, 92%, 91%, or 90%. In a non-limiting example, the PCM may have an energy storage efficiency from 92% to 99%, preferably 93% to 98%, preferably 94% to 97%, preferably 95% to 96%, or 96.5%. In some examples, the PCM may have an energy storage ability of at least 70%, preferably at least 68%, 66%, 64%, 62%, 60%, 58%, 56%, 54%, 52%, or 50%.
(56) Furthermore, the PCM may have a latent heat in a freezing process of at least 100 J/g, preferably at least 98 J/g, 96 J/g, 94 J/g, 92 J/g, 90 J/g, 88 J/g, 86 J/g, 84 J/g, 82 J/g, or 80 J/g and a latent heat in a melting process of at least 110 J/g, preferably at least 108 J/g, 106 J/g, 104 J/g, 102 J/g, 100 J/g, 98 J/g, 96 J/g, 94 J/g, 92 J/g, or 90 J/g. In a non-limiting example, the ss-PCM may have a latent heat value from 125 J/g to 175 J/g at a PEG to UiO-66 weight ratio of 0.5, preferably 130 J/g to 170 J/g, preferably 135 J/g to 165 J/g, preferably 140 J/g to 160 J/g, preferably 145 J/g to 155 J/g, or 150 J/g. Additionally, the PCM may have a freezing temperature of at least 35° C., preferably at least 34° C., 33° C., 32° C., 31° C., 30° C., 29° C., 28° C., 27° C., 26° C., or 25° C. and a melting temperature of at least 55° C., preferably at least 54° C., 53° C., 52° C., 51° C., 50° C., 49° C., 48° C., 47° C., 46° C., or 45° C.
(57) In some examples, the PCM may have an impregnation ratio of at least 60%, preferably at least 59%, 58%, 57%, 56%, 55%, 54%, 53%, 52%, 51% or 50% and an impregnation efficiency of at least 55%, preferably at least 54%, 53%, 52%, 51%, 50%, 49%, 48%, 47%, 46% or 45%. The impregnation ratio can be defined as the amount of polymer that is absorbed into the ss-PCM per unit volume of the ss-PCM. The impregnation efficiency is defined as the amount of polymer absorbed into the ss-PCM per unit volume of the ss-PCM per the amount of polymer used in total.
EXAMPLES
(58) The following examples describe and demonstrate exemplary embodiments of the method to form the PCM described herein. The examples are provided solely for the purpose of illustration and are not to be construed as limitations of the present disclosure, as many variations thereof are possible without departing from the spirit and scope of the present disclosure.
Materials
(59) 1,4-Benzenedicarboxylic acid, 2-amino-1,4-benzenedicarboxylic acid, DMF, and zirconium tetrachloride were used. Polyethylene glycol (MW 1000, 4000, 6000, and 10000) used as the PCM material and solvent ethanol were used as well. All chemicals were used without further purification.
Example 1
Synthesis of UiO-66
(60) UiO-66 was synthesized using a Hydrothermal Method. 1,4-Benzenedicarboxylic acid (100 mg, 0.6 mmol), and ZrCl.sub.4 (133.6 mg, 0.6 mmol) were dissolved in 40 mL of DMF and heated at 393 K for 24 h to form the UiO-66 PCM. The resulting UiO-66 was washed three times with DMF (5-10 mL) using a centrifuge (10000 rpm for 30 min), and then was sequentially treated with methanol (5-10 mL three times per day) for three 24 h periods. Finally, UiO-66 was activated by removing the solvent under vacuum for 24 h at 100° C.
Example 2
Synthesis of UiO-66-NH.SUB.2
(61) UiO-66-NH.sub.2 was synthesized by dissolving ZrCl.sub.4 (125 mg, 0.54 mmol) and 2-amino-1,4-benzenedicarboxylic acid (134 mg, 0.75 mmol) in DMF (20 mL) with ultrasonication for 30 min. The as-obtained mixture was transferred to a stainless-steel Teflon-lined autoclave of 50 mL capacity and heated at 393 K for 24 h. Then the autoclave was cooled in air to room temperature. The resulting solid was filtered, repeatedly washed with CHCl.sub.3, and dried at room temperature.
Example 3
Preparation of Composite PCM
(62) PEG-MOF, specifically PEG-UiO-66 PCM composite, was synthesized by dissolving varying amounts of PEG-6000 (1.0 g, 0.7 g, and 0.5 g) and 0.2 g of UiO-66 in 50 mL ethanol. PEG-6000 and UiO-66 were mixed well by stirring for 30 min. The mixture was then placed in an ultrasonication machine for another 30 min for further dissolution. The solution was allowed to stand at 80° C. for 24 h with stirring to remove the ethanol by evaporation. Finally, PEG-6000-1.0 g/UiO-66-0.2 g (PU-1.0), PEG-6000-0.7 g/UiO-66-0.2 g (PU-0.7), and PEG-6000-0.5 g/UiO-66-0.2 g (PU-0.5) composite PCM samples were obtained.
(63) In addition, composite PCM samples having PEG of different molecular weights, viz., PEG-1000-0.5/UiO66-0.2 g (PU-1000-0.5), PEG-4000-0.5/UiO66-0.2 g (PU-4000-0.5), and PEG-10000-0.5/UiO66-0.2 g (PU-10000-0.5) were also prepared.
(64) Further, composite PCM samples having CNTs, PEG-0.5 g/UiO-66-0.2 g-CNT 5 wt. % (PU-0.5-CNT 5 wt. %), and —NH.sub.2 functional groups, PEG-0.5 g/UiO-66-NH.sub.2-0.2 g (PU-NH.sub.2-0.5) were also prepared.
(65) The PCM samples prepared using PEG-6000 (PU-1.0, PU-0.7, PU-0.5) were then characterized, as described below. The properties of additionally prepared PCM samples (PU-1000-0.5, PU-4000-0.5, PU-10000-0.5, PU-0.5-CNT 5 wt. %, and PU-NH.sub.2-0.5) were also evaluated for comparison purposes.
Example 4
Powder X-Ray Diffraction (PXRD) Pattern Analysis
(66) The PXRD patterns were obtained using a Bruker D8 advance diffractometer system (Berlin, Germany). All data were collected at a scanning velocity of 3 min.sub.−1 in the range of 2θ=10-70°.
(67) Powder X-ray diffraction (PXRD) patterns are shown
(68) As seen in
(69) As seen in
(70) Further, as seen in
(71) Turning to
Example 5
Fourier-Transform Infrared (FTIR) spectroscopy
(72) A Bruker FTIR spectrometer (Berlin, Germany) was used to record the FTIR spectra.
(73) Referring to
(74) In
(75) In
(76) The spectra of the composites shown in
(77) The FTIR spectra of PU-0.5, PU-0.7, and PU-1.0 show that peaks due to UiO-66 as well as PEG-6000 are present. No new peaks are present, indicating that only physical mixing is taking place in well-mixed UiO-66 and PEG-6000 composites. When seen in combination with PXRD patterns, FTIR results indicate that PEG-6000 successfully penetrates the porous structure of UiO-66, without disturbing the crystalline structure of the MOF framework.
Example 6
(78) Morphology of the Composite PCM Samples was Analyzed Using Field Emission Scanning Electron Microscope (FESEM) imaging and Transmission Electron Microscope (TEM) imaging. FESEM (TESCAN LYRA3, Czech Republic) was used to determine the morphology and size of the particles. TEM images were obtained using a JEOL Inc., JEM 2011, with a CCD camera operating at 200 kV.
(79)
(80) As seen in
(81) As seen in
(82) Referring to
(83) Turning to
(84) As seen in
(85) Referring to
Example 7
Thermal Storage Properties
(86) The melting and freezing points and the latent heat of the composite PCM samples were determined using a DSC-Q2000. DSC data were collected by heating 8.5 mg of each sample sealed in an aluminum pan. DSC data were obtained under an argon gas flow rate of 20 mL/min at a heating rate of 5° C./min. The maximal deviations for phase change temperature and latent heat values determined based on the average of three measurements are ±0.11° C. and ±0.43 J/g, respectively.
(87) Referring to
(88) TABLE-US-00001 TABLE 1 Phase-change characteristics of the PEG and PEG/UiO-66 ss-PEM [PEG-6000 = PEG] phase change phase change Supercooling temperature (° C.) enthalpy ΔH(J/g) ΔT freezing melting freezing melting sample T.sub.f(° C.) T.sub.m(° C.) ΔH.sub.f(J/g) ΔH.sub.m(J/g) ΔT.sub.g(° C.) R % E (%) γ(%), φ (%) PEG 39.5 63.84 201 221.3 24.34 100 PEG-0.5 36.6 58.03 135 146 21.39 66 66.6 101 92.36 PU-0.7 34.2 56.67 130.2 134 22.42 63.5 64.1 100.8 88.85 PU-1.0 37.4 58.12 113.1 122 20.76 55.7 55.7 101 77.18 PU-0.5-CNT 42.2 61.69 119.1 120.9 19.53 52.1 54.2 104 76.48 PEG-10000 40.9 62.91 105 109.5 21.96 51.7 52 104 72.44 0.5/UiO-66 0.2 PEG-4000 36.8 56.98 119.5 122.8 20.2 58.3 58.8 101 81.6 0.5/UiO-66 0.2 PEG-1000 22.1 35.59 113.6 115.3 13.45 52.1 54.2 104 72.94 0.5/UiO-66 0.2 PEG- 41.5 59.07 107.6 110 17.53 49.7 51.5 103.7 6000.5/UiO- 66 NH.sub.2 0.2 T.sub.f = freezing temperature, T.sub.m = melting temperature, ΔH.sub.f = latent heat in freezing process, ΔH.sub.m = latent heat in melting process, ΔT = supercooling, R% = impregnation ratio, E (%) = impregnation efficiency, γ = heat storage efficiency, and φ = energy storage ability (capability), and blank cells indicate that data are not available.
(89) For the freezing and melting cycles, the enthalpies of PEG-6000 and the composites were determined using the region under the DSC curves. As seen in Table 1, PU-0.5 performs better with an impregnation ratio of 65.97% compared to 54.20% for PU-0.5-CNT 5 wt. %. The impregnation efficiency (E %) of PU-0.5 is also the highest among the tested samples. The thermal storage capacity of PU-0.5 composites indicates that almost all PEG-6000 molecules efficiently release/store energy through the transition of phases. The supercooling ΔT values are based on the difference between the freezing and melting temperatures, ΔTs of pure PEG-6000, PU-0.5, PU-0.7, and PU-1.0 is 24.34° C., 21.39° C., 22.42° C., and 20.76° C., respectively. The supercooling problem is overcome most likely due to the higher thermal conductivity. A high latent heat value of 146 J/g, the highest among the tested samples, was observed for the PU-0.5 sample. The high latent heat value of PU-0.5 indicates that the ss-PCM is a potential candidate to produce building materials to provide comfort in buildings. Among the tested samples, PU-0.5 also demonstrates the highest energy storage efficiency of 96.48%. Further, the highest amount PolyMOF is formed in the case of the PU-0.5 sample which may be playing a vital role in enhancing the latent heat storage capability.
Example 8
Pore the Size and Pore Volume
(90) The N.sub.2 adsorption-desorption isotherms were obtained at −196° C. using liquid N.sub.2. The pore size distribution was calculated using the Barrett—Joyner—Halenda formula. The sample powders were evacuated for 3 h at 200° C. Then the experiment was conducted at a heating rate of 5° C./min from room temperature to 600° C. under a dry nitrogen atmosphere. To assess the BET properties, i.e., pore size distribution, specific surface area etc., a NOVA-1200 device (JEOL U.S.A.) was used. A Tristar II 3020 system was employed to determine the BET surface area.
(91) The N.sub.2 adsorption-desorption isotherm of UiO-66, is shown in
(92) Typically, the performance of an ss-PCM depends on the porosity of the matrix which plays an important role in the polymer penetration process. The high pore volume of UiO-66 (micropore volume of 0.379 cm.sup.3g.sup.−1 and pore diameter of 18.96 Å) and the structure of the polyMOF plays a crucial role in the high latent heat of the PCMs based on UiO-66. These properties also increase the thermal stability of PU-0.5 PCM during melting and freezing cycles.
(93) Referring to
Example 9
Thermal Stability
(94) Thermogravimetric analysis (TGA) was performed using a Shimadzu thermal analyzer (TA-50). About 10 mg each of the PCM samples was used to perform TGA. The heating rate was maintained at 5° C./min from 25 to 600° C. under a dry nitrogen atmosphere.
(95) Referring to
(96) During the thermal decomposition, consecutive large weight losses occur from 220° C. to 460° C. The weight loss of porous UiO-66 is about 42.5% at 460° C. The successive weight losses can be due to dehydroxylation of —OH and the decomposition of the 1,4-benzene dicarboxylic acid and CO.sub.2. At the end of the decomposition, the remaining residue is mainly zirconium oxides derived from UiO-66. At about 78° C., pure PEG-6000 starts to melt. Sudden decomposition of pure PEG-6000 sample begins at about 400° C. and the total weight loss is 100% at about 440° C. In addition to the removal of absorbed water and hydroxyl groups from the matrix, the weight loss observed for PU-0.5 composite is due to the decomposition of organic molecules. A noteworthy aspect is that the total weight of PU-0.5 is 17% higher than that of pure PEG-6000, clearly indicating that PEG-6000 is thoroughly mixed and/or has penetrated the porous structure of UiO-66. Significant decomposition of PU-0.5 does not take place below 80° C. The composite PU-0.5 PCM demonstrates the thermal stability of the combination of UiO-66 and PEG-6000. By creating a self-protective barrier, the porous UiO-66 support can enhance the thermal stability of organic PEG-6000. The overall weight loss of the PU-0.5 composite is 78.2% at about 560° C. In the lower temperature range of 25° C. to 200° C., the weight loss of PU-0.5 is negligible.
Example 10
Thermal Cycling Properties
(97) The thermal cycling performance of the composite PU-0.5 PCM, which is important for determining its feasibility of commercial use, was also evaluated. PU-0.5 PCM is thermally stable even after 200 cycles and a DSC curve was recorded every 50 cycles. The DSC curves recorded during cycling of PU-0.5 PCM are depicted in
Example 11
Seepage Test
(98) The seepage test was performed using a sample disk and powders of UiO-66, PEG-6000, PU-0.5, and PU-0.5-CNT-5 wt. %. The UiO-66 powder did not melt after 10 min and even after 20 min. The same phenomenon was observed for the PU-0.5 sample. The microstructure of the PU-0.5 composite remained unchanged indicating the absence of leakage and even at 80° C. for 20 min, PU-0.5 powder did not melt. The weight of the PU-0.5 sample before and after heat treatment remained unchanged, indicating the absence of any weight loss. No leaks were observed in the leakage test performed for the PU-0.5-CNT 5 wt. % sample either.
Example 12
Thermal Conductivity
(99) Thermal conductivity of the sample powders was determined using circular disk samples with a TCi Conductivity Analyzer, Canada. The equipment uses modified transient plane source (MTPS) and the measurement method is based on C-Therm Technologies.
(100) The thermal conductivity of UiO-66 alone is 0.84 W/mK, while the thermal conductivity of PEG-6000 alone is 0.22 W/m K. A relatively high thermal conductivity of 0.52 W/mK was observed for the PU-0.5 PCM. This result is very promising considering that material with a higher conductivity has a high demand in the field of solar energy storage and its application can enhance the charging and discharging rates.