METHOD FOR SYNTHESIS OF ORGANIC IODIDES, A PEROVSKITE-FORMING COMPOSITION COMPRISING AN ORGANIC IODIDE AND A PHOTOVOLTAIC CELL WITH A PEROVSKITE LAYER OBTAINED THEREFROM
20220185765 · 2022-06-16
Inventors
- Kasjan MISZTAL (Wroclaw, PL)
- Konrad WOJCIECHOWSKI (Wroclaw, PL)
- Olga MALINKIEWICZ (Wroclaw, PL)
- Zbigniew MIARA (Dankowice, PL)
Cpc classification
C07C209/00
CHEMISTRY; METALLURGY
B01J31/0235
PERFORMING OPERATIONS; TRANSPORTING
C07C211/07
CHEMISTRY; METALLURGY
C07C211/07
CHEMISTRY; METALLURGY
H10K30/00
ELECTRICITY
C07C209/00
CHEMISTRY; METALLURGY
C07C257/12
CHEMISTRY; METALLURGY
C01P2002/72
CHEMISTRY; METALLURGY
H10K30/10
ELECTRICITY
H01G9/2059
ELECTRICITY
International classification
C07C209/00
CHEMISTRY; METALLURGY
B01J31/02
PERFORMING OPERATIONS; TRANSPORTING
C07C257/12
CHEMISTRY; METALLURGY
Abstract
A method for obtaining a salt with a general formula: R.sub.xNI, wherein: R.sub.xN is an organic cation (R.sub.xN.sup.+), R represents substituents (R−) independently selected from a group consisting of organic substituents: R.sup.1−, R.sup.2—, R.sup.3— and hydrogen (H—), x is a number of the substituents R— directly linked with the nitrogen (N) atom in the organic cation R.sub.xN.sup.+, wherein x is 3 or 4, I is an iodide anion (I.sup.−). The method comprises: preparing a reaction mixture comprising the steps of: synthesizing hydrogen iodide (HI) in situ by mixing molecular iodine (I.sub.2) with formic acid (COOH) in a molar ratio of molecular iodine (I.sub.2): formic acid (COOH) of no less than 1.01:1, in a solvent medium, introducing into the solvent medium a compound being a donor of organic cation R.sub.xN.sup.+ in an amount providing the molar ratio of the donor of organic cation R.sub.xN.sup.+: molecular iodine (I.sub.2) of no less than 1.01:1, and maintaining the reaction mixture at a temperature of not less than 20° C. for the time necessary to obtain the reaction product being the salt with the general formula R.sub.xNI. The obtained product is a substrate for synthesis of perovskites.
Claims
1. A method for obtaining a salt having a general formula: R.sub.xNI, wherein: R.sub.xN is an organic cation (R.sub.xN.sup.+), wherein R represents substituents (R—) independently selected from a group consisting of organic substituents: R.sup.1—, R.sup.2—, R.sup.3— and hydrogen (H—), wherein the donor of organic cation R.sub.xN.sup.+ contains as organic substituents: R.sup.1—, R.sup.2— and optionally R.sup.3— moieties independently selected from a group consisting of: straight chain or branched chain alkyl substituents containing 1 to 8 carbon atoms in a substituent molecule, x is a number of the substituents R— directly linked with the nitrogen (N) atom in the organic cation R.sub.xN.sup.+, wherein x is 3 or 4, I is an iodide anion (I.sup.−), the method comprising the steps of: preparing a reaction mixture by: synthesizing hydrogen iodide (HI) in situ by mixing molecular iodine (I.sub.2) with formic acid (COOH) in a molar ratio of molecular iodine (I.sub.2): formic acid (COOH) of no less than 1.01:1, in a solvent medium, introducing into the solvent medium a compound being a donor of an organic cation R.sub.xN.sup.+ in an amount providing the molar ratio of the donor of the organic cation R.sub.xN.sup.+: molecular iodine (I.sub.2) of no less than 1.01:1, and maintaining the reaction mixture at a temperature of not less than 20° C. for a time necessary to obtain a reaction product being the salt having the general formula R.sub.xNI.
2. (canceled)
3. The method according to claim 1, wherein molecular iodine (I.sub.2) is mixed with formic acid (HCOOH) at a molar ratio: molecular iodine (I.sub.2): formic acid (COOH) of 1.01:1 to 1.1:1, and the donor of the organic cation R.sub.xN.sup.+ is introduced to the solvent medium in an amount providing a molar ratio of the donor of organic cation R.sub.xN.sup.+: molecular iodine (I.sub.2) of 1.01:1 to 1.50:1.
4. The method according to claim 1, wherein molecular iodine (I.sub.2) is mixed with formic acid (HCOOH) at a molar ratio of iodine (I.sub.2): formic acid (COOH) of 1.01:1.
5. The method according to claim 1, wherein the reaction mixture is heated to a temperature in a range from 20 to 80° C.
6. The method according to claim 1, wherein the donor of the organic cation R.sub.xN.sup.+ is introduced to the solvent medium following the synthesis in situ of hydrogen iodide (HI).
7. The method according to claim 1, wherein amine is used as a donor of the organic cation R.sub.xN.sup.+, and the obtained salt (R.sub.xNI) contains the organic cation (R.sub.xN.sup.+) selected from the group consisting of: alkylammonium cations (R(H.sub.3)N.sup.+), dialkylammonium cations R.sub.2(H.sub.2)N.sup.+, and trialkylammonium cations (R.sub.3(H)N.sup.+).
8. The method according to claim 7, wherein primary alkylamine with the general formula RNH.sub.2 is used as the donor of organic cation R.sub.xN.sup.+, and the obtained salt: alkyl ammonium iodide has the general formula of R(H.sub.3)NI, where the substituent R represents an alkyl moiety containing 1 to 8 carbon atoms.
9. The method according to claim 7, wherein methylamine is used as the donor of organic cation R.sub.xN.sup.+, and methylammonium iodide (MAI) is obtained as the salt.
10. The method according to claim 7, wherein octylamine is used as the donor of organic cation R.sub.xN.sup.+, and octylammonium iodide (OAI) is obtained as the salt.
11. The method according to claim 1, wherein an amidine salt is used as the donor of organic cation R.sub.xN.sup.+ and amidinium iodide (R.sub.2N—(R.sup.3)C═N(H.sub.2(I) is obtained as the salt.
12. The method according to claim 11, wherein formamidine acetate is used as the donor of organic cation R.sub.xN.sup.+ and formamidinium iodide (FAI) (H.sub.2N—C(H)═N(H.sub.2)I) is obtained as the salt.
13. The method according to claim 1, wherein the solvent medium comprises at least one compound selected from a group consisting of: methanol, ethanol, absolute ethanol, isopropanol, dioxane, tetrahydrofuran (THF) and dimethylformamide (DMF).
14. The method according to claim 9, wherein the solvent medium is water.
15. The method according to claim 1, wherein preparing a reaction mixture further comprises the step of introducing, into the solvent medium, a catalyst being a salt with the general formula R.sub.xNI.
16. The method according to claim 15, wherein the catalyst is a compound identical to the salt R.sub.xNI being the reaction product.
17. (canceled)
18. The method according to claim 15, wherein the catalyst is introduced at a molar ratio of catalyst: molecular iodine (I.sub.2) ranging from 0.01:1 to 0.03:1.
19. Use of the salt having the general formula: R.sub.xNI prepared by using the method according to claim 1, as a substrate in a synthesis of perovskites.
20. A perovskite-forming composition, comprising the salt with the general formula: R.sub.xNI obtained using the method according to claim 1.
21. The perovskite-forming composition according to claim 20, comprising the salt with the general formula: R.sub.xNI selected from the group consisting of: methylammonium iodide (MAI), ethylammonium iodide, propylammonium iodide, butylammonium iodide, pentylammonium iodide, hexylammonium iodide, heptylammonium iodide, octylammonium iodide (OAI) and formamidinium iodide (FAI).
22. The perovskite-forming composition according to claim 21, further comprising at least one lead salt and at least one solvent.
23. The perovskite-forming composition according to claim 18, further comprising methylammonium dihydrogen phosphate (I) CH.sub.3NH.sub.3H.sub.2PO.sub.2.
24. The perovskite-forming composition according to claim 23, comprising the following compounds: methyl ammonium iodide (MAI), anhydrous lead (II) acetate (CH.sub.3COO).sub.2Pb and lead (II) chloride PbCl.sub.2 in the amounts effective for the synthesis of perovskite from said compounds, as well as dimethylformamide (DMF) as a solvent and methyl ammonium dihydrogen phosphate (I) CH.sub.3NH.sub.3H.sub.2PO.sub.2 in the amount of 0.3% by weight with respect to the weight of methylammonium iodide (MAI) contained in the composition.
25. The perovskite-forming composition according to claim 21, comprising formamidinium iodide (FAI), methylammonium bromide CH.sub.3NH.sub.3Br, lead (II) iodide PbI.sub.2 and caesium iodide (CsI), in the amounts effective for the synthesis of perovskite from said compounds.
26. A photovoltaic cell comprising a perovskite layer prepared using the salt with the general formula: R.sub.xNI, that is obtained using the method according to claim 1.
27. (canceled)
28. The method according to claim 1, wherein wherein R represents substituents (R—) independently selected from a group consisting of organic substituents: R.sup.1—, R.sup.2—, R.sup.3— and hydrogen (H—), wherein the donor of organic cation R.sub.xN.sup.+ contains as organic substituents: R.sup.1—, R.sup.2— and optionally R.sup.3— moieties independently selected from a group consisting of: straight chain or branched chain alkyl substituents containing 1 to 8 carbon atoms in a substituent molecule, and at least one heteroatom substituting the carbon atom or hydrogen atom in the substituent molecule, wherein the heteroatom is selected from the group consisting of: silicon, oxygen, nitrogen, sulphur, iodine, chlorine and bromine.
Description
[0045] The object of the invention is shown in exemplary embodiments in the drawing where:
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[0064] The developed method according to the invention allows for preparing a group of chemical compounds to be used as perovskite precursors, which are salts with the general formula R.sub.xN, and in the ion notation: RxN.sup.+I.sup.−, where R.sub.xN.sup.+ is an organic cation, I.sup.− is an iodide anion, and x is the number of substituents directly linked to the nitrogen atom, preferably x is from 3 to 4 (if x=3 a double bond in the organic cation exists between the nitrogen atom and the carbon atom in one R moiety).
[0065] The developed method for preparing R.sub.xNI compounds ensures improved purity of the obtained products, which in turn enable for using them as perovskite precursors in various perovskite-forming compositions, including colloidal solutions, such as inks, for producing perovskite coatings with improved morphology and quality of perovskite crystals.
[0066] The developed method of the iodide synthesis differs from the prior art methods in that the method according to the present disclosure involves the step of obtaining hydrogen iodide (HI) in situ in the reaction medium. In other words, according to the is developed method, hydrogen iodide (HI) is not used as a direct substrate for the synthesis of the respective iodides, Instead, the developed method comprises the step of supplying, into the reaction medium, the substrates that are suitable for in situ hydrogen iodide (HI) synthesis.
[0067] The developed method allows for obtaining various compounds which are iodide salts with the molecular formula R.sub.xNI, wherein organic cation R.sub.xN.sup.+ is selected from a group consisting of: [0068] ammonium cations with the general formula: R.sub.4N.sup.+ (x=4), including alkylammonium cations: R.sup.1(H.sub.3)N.sup.+, dialkylammonium cations: R.sup.1R.sup.2(H.sub.2)N.sup.+ and trialkylammonium cations: R.sup.1R.sup.2R.sup.3(H)N.sup.+, and [0069] ammonium cations with the general formula: R.sub.3N.sup.+ (x=3), including amidinium cations: R.sup.1R.sup.2N—(R.sup.3)C═N(H.sub.2).sup.+, and formamidinium cations: R.sup.1R.sup.2N—C(H)═N(H.sub.2).sup.+, wherein moiety: R— is selected from the group: H—, R.sup.1—, R.sup.2— and R.sup.3—, in accordance with the general formulas of cations as indicated above. The substituents R—, R.sup.1—, R.sup.2—, R.sup.3— may be the same or different moieties selected from a group consisting of: hydrogen (H—), straight chain and/or branched aliphatic hydrocarbons (C.sub.yH.sub.z—), alicyclic hydrocarbons, including saturated hydrocarbons and/or containing an unsaturated bond or bonds, and aromatic hydrocarbons, Preferably, every substituent: R—R.sup.1—, R.sup.2—, R.sup.3— of organic cation (R.sub.xN.sup.+), other than (H—) may contain 1 to 8 carbon atoms in the molecule, i.e. for at least one substituent: R—R.sup.1—, R.sup.2—, R.sup.3— with the general formula C.sub.yH.sub.z—, y may be: 1÷8. Also, at least one substituent: R.sup.1—, R.sup.2—, R.sup.3— of the organic cation may have at least one atom of carbon or hydrogen substituted with another atom, for example: silicon, oxygen, nitrogen, sulphur, iodine, chlorine or bromine.
[0070] For example, the developed method may be used to obtain iodide salts (R.sub.xNI), wherein the organic cation (R.sub.xN.sup.+), [0071] for x=4, is methylammonium CH.sub.3(H.sub.3)N.sup.+, ethylammonium CH.sub.3CH.sub.2(H.sub.3)N.sup.+, propylammonium C.sub.3H.sub.7(H.sub.3)N.sup.+, butylammonium C.sub.4H.sub.9(H.sub.3)N.sup.+, pentylammonium H.sub.3C.sub.5H.sub.11N.sup.+, hexylammonium H.sub.3C.sub.6H.sub.13N.sup.+, heptylammonium C.sub.7H.sub.15(H.sub.3)N.sup.+ or octylammonium C.sub.8H.sub.17(H.sub.3)N.sup.+ cation, [0072] and for x=3, is formamidinium (H.sub.2N—HC═NH.sub.2).sup.+, or guanidinium (H.sub.2N).sub.2—C═NH.sub.2).sup.+ cation.
[0073] For greater clarity, examples of iodides salts, which may be obtained using the inventive method, are shown, in a form of structural and semi-structural formulae, in
[0074] Thus, the developed method enables one to obtain iodide salts R.sub.4NI (
[0075]
[0080] Depending on the target synthesis product, various organic compounds may be used as the donors of organic cation R.sub.xN.sup.+ i.e. the compounds that are capable of dissociation in the reaction medium to form a respective organic cation: R.sub.xN.sup.+, i.e. a cation selected from the group: R.sub.4N.sup.+ and R.sub.3N.sup.+.
[0081] Preferably, compounds whose dissociation does not involve introducing additional, and difficult to remove, contaminations to the reaction medium are used as the donors of organic cation R.sub.xN.sup.+.
Examples of Compounds to be Used as the Donor of Organic Cation R.sub.xN.sup.+ According to the Developed Method for Preparing R.sub.xNI Salts:
[0082] For example, amines, preferably primary amines, and preferably containing 1 to 8 carbon atoms in the molecule, such as methylamine (CH.sub.3NH.sub.2) to obtain methylammonium iodide (CH.sub.3NH.sub.3I), ethylamine (C.sub.2H.sub.5NH.sub.2) to obtain ethylammonium iodide (C.sub.2H.sub.5NH.sub.3I) or octylamine (C.sub.3H.sub.17NH.sub.2) to obtain octylammonium iodide (C.sub.8H.sub.17NH.sub.3I), may be used as the donor of organic cation R.sub.4N.sup.+ (i.e. x=4). The respective amines will therefore dissociate, yielding the respective organic cation R.sub.4N.sup.+ being the substrate for salt synthesis.
[0083] Furthermore, amidine acetates, such as formamidine acetate, may be used as the donor of organic cation R.sub.3N.sup.+ (i.e. x=3): (with the formula in ion notation: [(HC(NR)).sub.2).sub.2].sup.+[CH.sub.3COO].sup.−), since these compounds readily dissolve under reaction conditions and dissociate to the respective organic cations R.sub.3N.sup.+ and acetate anion, which, in the course of the reaction, is converted to acetic acid and which, due to its low boiling point, can be evaporated from the solution and thus easily removed from the post-reaction mixture.
[0084] The above-mentioned selection of a compound serving as the donor of organic cation provides high purity of synthesis product, i.e. a salt containing an iodide anion and an organic cation, so that the quality of perovskite coatings made with the salt R.sub.xNI prepared using the developed method is improved.
[0085] Depending on the solubility of the donor of organic cation R.sub.xN.sup.+ used, the reaction may be carried out in polar or apolar medium, with various solvents providing good solubility of molecular iodine (I.sub.2) (reactions presented in
[0086] For example, in the embodiment of the disclosure with methylamine used as the donor of organic cation, the reaction can be carried out in a solvent such as water, methanol, ethanol, absolute ethanol (at a concentration of 99.8%, for example, obtained by distillation with added benzene; the contamination of the solvent with a small amount of benzene does not adversely affect the final purity of the product, since it may be removed in the course of purification), isopropanol, a mixture of suitable alcohol with water, dioxane, tetrahydrofuran (THF), wherein the reaction is preferably carried out using absolute ethanol as the solvent, since absolute ethanol provides relatively high solubility of substrates including molecular iodine and the donors of organic cation, including methylamine. Furthermore ethanol has a boiling point of 78° C., thus allowing the reaction to be carried out at preferred temperature of over 50° C. Moreover, absolute ethanol is easily removable in the course of the purification of the reaction product.
[0087] Together with the increase of the number of carbon atoms in the molecule of the donor of organic cation, the polar character of the molecule weakens in favor of non-polar character of the molecule, This imposes using, instead of water, solvents such as methanol, ethanol, isopropanol, absolute ethanol, dioxane, tetrahydrofuran (THF).
[0088] For example, where octylamine or formamidine acetate is used as the donor of organic cation, ethanol may be used as the solvent.
[0089] Introduction of the donor of organic cation in the course of preparation of the reaction mixture, is preferably accomplished at the temperature from the range of 0 to 30° C. For example, the addition of the donor of organic cation may be accomplished at room temperature, since the reaction triggered by such the addition is exothermic by nature. After adding the compound being the donor of organic cation, the reaction mixture is heated preferably to the temperature exceeding 50° C. This ensures an increase in the reaction rate. In such temperature conditions the reaction can be is carried out within a relatively short period of time, e.g., less than 2 hours, with satisfactory product yield.
[0090]
[0091] As illustrated in
[0092] The reaction is carried out with an excess of iodine (I.sub.2) with respect to formic add (HCOOH), wherein, preferably, in the reaction there is used an excess of iodine at a molar ratio from 1.01 (I.sub.2): 1.0 (HCOOH) to 2.0 (I.sub.2): 1.0 (HCOOH) and more preferably, molecular iodine (II.sub.2) is used in excess at a molar ratio with respect to formic acid of 1.01 (I.sub.2): 1.0 (HCOOH) to 1.10 (I.sub.2): 1 (HCOOH), and most preferably at a molar ratio of 1.05 (I.sub.2) 1 (HCOOH).
[0093] The excess of molecular iodine with respect to formic acid in the reaction medium provides the synthesis of respective iodide salt with improved (superior) purity.
[0094] Even a small excess of iodine (I.sub.2) with respect to formic acid (HCOOH), and more preferably an excess of I.sub.2 with respect to HCOOH in the range indicated above, prevents the formation in the reaction mixture of by-products being formates of respective organic cations ([R.sub.xN.sup.+][HCOO.sup.−]), whose donors are added to the reaction mixture. Such salts ([R.sub.xN.sup.+][HCOO.sup.−]), are difficult to separate from the reaction product, and in some cases (of specific salts and specific products) it is impossible without using costly specialised purification methods. Therefore, it is advantageous to use molecular iodine in appropriate excess.
[0095] The use of molecular iodine in excess with respect to formic acid always improves the purity of the obtained product by limiting the formation of hard-to-remove by-products ([R.sub.xN.sup.+][HCOO.sup.−]), wherein the most advantageous molecular iodine excess, providing a substantial reduction in the formation of reaction by-products of hard-to-remove salts ([R.sub.xN.sup.+][HCOO.sup.−]) is from 1.01 to 1.10 mole I.sub.2 per 1 mole HCOOH.
[0096] Further, in order to remove iodine present in the post-reaction mixture, the product needs to be purified, and if an excess of iodine used is higher than indicated, the purification procedure may need to be repeated (recrystallization), which generates additional costs due to the use of additional solvents, which is also time-consuming.
[0097] Consequently, in order to prevent contamination of the final product with both the excess of unreacted iodine and reaction by-products in a form of acetic acid salts ([R.sub.xN.sup.+][HCOO.sup.−]), a preferred excess of iodine which may be used is 1.01 mole I.sub.2 per 1 mole HCOOH, such value provides optimally high purity of the final product.
[0098] Moreover, the reaction is carried out in an excess of the donor of organic cation (R.sub.xN.sup.+) (examples of which are indicated above) with respect to molecular iodine (I.sub.2), wherein the most preferred excess of the donor of organic cation with respect to molecular iodine is in the range of 1.01 to 1.50 mole of the donor of organic cation for each 1 mole of molecular iodine (I.sub.2). The use of an excess of the donor of organic cation provides the advantages described below. Inter alia, the excess of organic s cation (R.sub.xN.sup.+) with respect to molecular iodine ensures complete reaction of the hydrogen iodide (HI), obtained in-situ, with the organic cation. If the obtained HI remained in the reaction environment, resulting from a molar deficit of the donor of organic cation, at the end of the reaction, this remained acid HI might undergo oxidation to iodine oxoacids such as: HIO, HIO.sub.2, HIO.sub.3 and HIO.sub.4, so that by-products (in a form of respective salts) might be formed through anion-exchange reactions between the iodine oxoacids and the reaction product. Such salts would be very difficult to separate from the product, resulting in lower purity of the product (the respective iodide salt). Therefore, in order to prevent an excess of hydrogen iodide (HI) prepared in situ with respect to the donor of organic cation an excess of the donor of organic cation (R.sub.xN.sup.+) is used, and this prevents the contamination of the reaction product, as explained above. In other words, the excess of organic cation (R.sub.xN.sup.+) with respect to the amount of molecular iodine (I.sub.2) added to the reaction medium ensures improved purity of the product obtained. Moreover, for the embodiments according to the present disclosure, in which the donor of organic cation (R.sub.xN.sup.+) is in a gas or liquid state, at the given reaction conditions, unreacted excess of said compound may be easily separated from the reaction product using commonly known purification techniques.
[0099] An additional advantage of providing an excess of the donor of organic cation (R.sub.xN.sup.+), at the preparation of the reaction mixture, is a relatively low price of the mentioned compounds (such as methylamine) comparing to the price of molecular iodine (I.sub.2), which means a reduction in the cost of preparing respective iodides using the developed method.
[0100] Optionally, in order to achieve improved time efficiency, the reaction of the synthesis of the salt R.sub.xNI may be carried out with the presence of a small amount of catalyst, being a compound, preferably, identical to the R.sub.xNI iodide salt being the reaction product. Reactions with the use of respective catalyst are shown in
[0101] Thus, similar to the steps of synthesis of the respective iodides: MAI, OAI and FAI, without catalyst (
[0102] As may be seen in
[0103] I.sub.3.sup.− ions, formed with the catalyst added to the reaction, feature greatly improved solubility, in polar solvents, and they react more readily with formic acid HCOOH, yielding hydrogen iodide (HI) in situ, when compared to that of molecular iodine (I.sub.2), which is slightly less prone to react with formic acid with obtaining hydrogen iodide (HI) in situ. Thus, the addition of a catalyst (
[0104] Since the formation of a transition form: a three-atom iodine anion: I.sub.3.sup.− has an accelerating effect, the reaction with the presence of the catalyst can be carried out e.g. on an industrial or semi-technical scale, thus increasing the production capacity of said compounds.
[0105] The addition of the catalyst reduces the reaction time by approximately 60 to 180 minutes. Thus, with added catalyst, the average reaction time is 20 to 120 minutes, while without catalyst, the average reaction time is 120 to 300 minutes.
[0106] An additional advantage of using the catalyst being the same compound as the product of the reaction is improved purity of the resulting product as the catalyst and the reaction product are the same compounds, thereby the catalyst does not constitute contamination of the product. However, using as the catalyst a iodide salt, preferably R.sub.xNI, which is not the same compound as the synthesised product, will also increase the reaction rate.
[0107] Preferably, the catalyst is added to the system in an amount of 0.01 to 0.03 mole per each mole of molecular iodine (II.sub.2), i,e. in the molar ratio of 0.01 (mole of the catalyst): 1 (mole of I.sub.2) to 0.03 (mole of the catalyst): 1 (mole of I.sub.2). The reaction with the presence of catalyst is carried out at a temperature ranging from 0 to 80° C.
[0108] Thus, in the MAI synthesis, MAI may be preferably used as the catalyst, in the OAI synthesis, OAI may be preferably used as the catalyst, and in the FAI synthesis, FAI may be preferably used as the catalyst.
[0109] R.sub.xNI iodides salts obtained using the developed method feature improved product purity and are suitable e.g. to be used as one of the precursor components of the respective perovskite, in perovskite-forming compositions, for example, such as perovskite inks for printing on various substrates, such as: ITO, to prepare perovskite photoactive layers in photovoltaic cells.
[0110] The use of R.sub.xNI iodides obtained using the inventive method in perovskite-forming compositions, especially those used in photovoltaics in photoactive layers, is particularly advantageous, This is because the R.sub.xNI iodides obtained, used as one of the substrates in the synthesis of perovskites, ensure the formation of a perovskite layer exhibiting improved morphology, resulting in improved photoactive properties of the resulting perovskite layer.
[0111] Preferably, the obtained products (R.sub.xNI) are recrystallized to isolate them from unreacted substrates used in the synthesis.
[0112]
[0113] Thus, iodides prepared using the developed method can be used to obtain various perovskites, including in particular those used in photovoltaics, for photoactive layers.
[0114] The iodides obtained using the developed method, due to their high purity, are suitable to be used in perovskite-forming compositions as precursor components of perovskites (for example, in accordance with the reactions in
[0115] Moreover, in the course of further research, the results of which are discussed lo below in the embodiments of the invention, it was found that a particularly advantageous perovskite-forming composition in a form of a colloidal solution is the composition containing iodide salt obtained using the developed method and added methylammonium dihydrogen phosphate (I) CH.sub.3NH.sub.3H.sub.2PO.sub.2 is especially suitable, since the perovskite-forming layers obtained with this composition provide improved Is parameters of the photovoltaic cell obtained therewith.
Embodiments
EXAMPLE I
Synthesis of Methylammonium Iodide (MAI), using MAI as a Catalyst
[0116] In a round-bottomed flask, a portion of MAI catalyst was dissolved in ethanol, adding MAI in an amount of 0.01 mole with respect to each I.sub.2 iodine mole to obtain a bright, translucent solution. Then, a whole portion of I.sub.2 iodine, dark brown in colour, was added to the resulting solution in a single step to obtain a brown, non-translucent solution, which confirmed the presence of iodine (I.sub.2) in the solution. After 5 minutes, this dissolved, which demonstrated that I.sub.3.sup.− were formed in the solution (otherwise I.sub.2 molecular iodine would dissolve at a much lower rate). Formic acid was then added to the resulting mixture in a single step, in molar ratio with respect to I.sub.2 iodine of 0.97:1.0, and macroscopically, no changes were observed in the flask, Methylamine, a donor of suitable organic cations, was then added to the solution. Methylamine was slowly added dropwise to the solution, making a total of 2.6 moles of methylamine per each mole of I.sub.2 iodine added to the solution. When adding methylamine, the formation of gas bubbles and foaming of the flask content was observed, which indicated that CO.sub.2 gas was released from the reaction mixture. During the reaction, an increase in temperature was also observed, which indicates that the reaction is exothermic. Bubble formation was observed only after adding methylamine, which can be explained by the fact that the use of hydrogen iodide (HI) produced in situ significantly accelerates the reaction. After completed adding of methylamine, the brown mixture was heated for 1 hour while maintaining the temperature of the mixture at 80° C., after which the reaction was terminated. After 1 hour of heating, the mixture turned pale brown from brown; however, the colour of the mixture was not considered to be an indicator of the termination of the reaction, due to the excess of iodine used with respect to formic acid, preventing the conversion of the whole content of iodine (I.sub.2) into hydrogen iodide (HI). The excess iodine used added to the reaction prevented the formation of methylammonium formate as a by-product of the reaction. The obtained product was isolated by evaporation of the solvent from the post-reaction mixture to obtain a yellow and brown powder, which was completely dissolved in boiling absolute ethyl alcohol (100%) for recrystallization. After cooling to room temperature, diethyl ether was added to the mixture to precipitate more product. The precipitate was filtered and washed with diethyl ether until the precipitate turned white. The resulting precipitate being the product of the reaction, i.e. MAI, was vacuum dried for 5 hours (pressure below 0.2 mbar), after which the product was weighed. A product (MAI) yield of 88% was obtained, comparing to the theoretical yield as per the stoichiometry of the reaction. The composition of the resulting product was subjected to analysis which confirmed the absence of even trace amounts of phosphorus salts since no phosphorus donors were used at any step of the synthesis.
[0117] The resulting product was also tested for the presence of phosphorus, and the results obtained were compared with MAI prepared using a method known in the art as well as commercially available MAI. The results are summarized in Table I.
EXAMPLE II
Synthesis of Octylammonium Iodide (OAI) Without Catalyst
[0118] A portion of iodine (I.sub.2) was dissolved in ethanol in a round-bottomed flask in a single step to obtain a non-translucent dark brown solution demonstrating the presence of molecular iodine (I.sub.2). After 15 minutes, the iodine dissolved in ethanol with the solution remaining dark brown and non-translucent. Formic acid was then added to the flask, in the molar ratio HCOOH:I.sub.2 of 0.97:1.0 with no changes observed in the flask. 2.6 moles of octylamine per each mole of I.sub.2 iodine were then slowly added dropwise to the solution. After adding each drop of octylamine, gas bubbles and foam appeared in the reaction solution, and the temperature of the reaction mixture was observed to increase due to its exothermic course. Gas bubbles and foam demonstrated that octylamine reacted with hydrogen iodide HI produced in situ. After adding total octylamine (the reaction mixture remained brown), the flask was heated for 2 hours while maintaining the temperature of the reaction mixture at 80° C. The reaction was then terminated, and the resulting mixture had a lighter brown colour, however, the colour of the mixture was not considered to be an indicator of the termination of the reaction due to the excess iodine (I.sub.2) used, which prevented it from being completely reacted. The use of excess iodine with respect to formic acid prevented the formation of octylamine formate, which would be a by-product of the synthesis, and thus a contamination of the resulting octylammonium iodide (OAI). When the reaction was over, the mixture was evaporated on a rotary evaporator under reduced pressure of 30 mbar, keeping the flask with the solution, during the evaporation, in water bath of temperature 50° C., to obtain as a result of the evaporation a yellow and brown powder which was then dissolved in boiling absolute ethanol for recrystallization in 1 mL of absolute ethanol per 1 g of the expected product (the assumed yield was 1 mL/1 g). The solution was then cooled and diethyl ether was added to the cooled mixture to increase the precipitation efficiency. This was filtered to obtain a white precipitate, which was washed with diethyl ether until the precipitate turned white. The resulting precipitate constituting the reaction product (OAI) was vacuum dried (pressure below 0.2 mbar) for 5 hours, after which the product was weighed. A product (OAI) yield of 76% was obtained, comparing to the theoretical yield as per the stoichiometry of the reaction.
EXAMPLE III
Synthesis of Formamidinium Iodide (FAI) Without Catalyst
[0119] A portion of iodine (I.sub.2) was dissolved in ethanol in a round-bottomed flask in a single step to obtain a non-translucent dark brown solution demonstrating the presence of molecular iodine (I.sub.2). After 15 minutes, the iodine dissolved in ethanol with the solution remaining dark brown and non-translucent. 1.0 Eq (equivalent) of formic acid HCOOH (with respect to iodine (I.sub.2)) was then added to the flask with no changes observed in the flask. Formamidine acetate (solid at room temperature) was then added to the solution in a single step in a total amount of 2.1 Eq (equivalents) of formamidine acetate (with respect to iodine (I.sub.2)). After adding formamidine acetate (the reaction mixture remained brown), the flask was heated for 12 hours, maintaining the reaction mixture temperature at 50° C. The reaction was then terminated, and the resulting mixture had a lighter brown colour. When the reaction was over, the mixture was evaporated on a rotary evaporator under reduced pressure of 30 mbar, keeping the flask with the solution being evaporated in a 50° C. water bath to obtain as a result of the evaporation a yellow and brown powder which was then dissolved in boiling absolute ethanol for recrystallization in 1 mL of absolute ethanol per 1 g of the expected product (the assumed yield was 1 mL/1 g). The solution was then cooled to room temperature and diethyl ether was added to the cooled mixture to increase the precipitation efficiency, This was filtered to obtain a white precipitate, which was washed with diethyl ether until the precipitate turned white. The resulting precipitate constituting the reaction product (FAI) was vacuum dried (pressure below 0.2 mbar) for 5 hours, after which the product was weighed. A product (FAI) yield of 82% was obtained, comparing to the theoretical yield as per the stoichiometry of the reaction.
[0120] The resulting product was also tested for the presence of phosphorus. The results are summarized in Table I below.
TABLE-US-00001 TABLE I Phosphorus MAI/FAI purity (P) content (with respect to [%] iodine content [%]) MAI (obtained using a known 0.281 97.26 method, without recrystallization) MAI (obtained using a known 0.041 98.05 method, double recrystallization) MAI (according to the 0% (not 99.47 disclosure) detected) MAI (commercially available, 0.486 93.61 manufacturer I) MAI (commercially available, 0.688 92.37 manufacturer II) FAI (according to the 0% (not 99.50 disclosure) detected)
EXAMPLE IV
Preparation of a Perovskite-Forming Composition in a Form of Ink, using MAI as the Perovskite Precursor
[0121] The perovskite-forming composition was prepared by dissolving the following compounds in 954 4 of dimethylformamide (DMF): [0122] 305.14 mg of methylammonium iodide (MAI) prepared according to the procedure of Example I above, [0123] 166.50 mg of anhydrous lead (II) acetate Pb(CH.sub.3COO).sub.2, [0124] 35.58 mg lead (II) chloride PbCl.sub.2 [0125] solution of dihydrogen phosphate (I) methylammonium CH.sub.3NH.sub.3H.sub.2PO.sub.2 in DMF at a concentration of 19.8 mg/mL in the amount of 46 4 (corresponding to 0.3% CH.sub.3NH.sub.3H.sub.2PO.sub.2 by weight with respect to the weight of MAI used).
[0126] The ingredients were mixed for 12 hours, after which the resulting colloidal solution was filtered using a 0.45 μM filter to obtain a colloid with a suitable particle size of the dispersed phase.
[0127] The resulting composition had the form of a stable colloid, suitable for printing (ink). No changes in colloidal particle sizes and no agglomeration tendency have been observed. During several weeks of observation the composition remained in form of a clear (translucent) colloidal solution.
[0128] The obtained colloid (containing single-crystallized MAI) is shown in the images: I, II, III, IV,
[0129] All photographs of
[0130] Thus, the perovskite-forming composition prepared in the form of a colloidal solution contains the inventive MAI as one of the perovskite-forming ingredients.
EXAMPLE V
Preparation of Perovskite Coatings Using MAI
[0131] Three perovskite-forming compositions were prepared as follows: [0132] composition I, containing ingredients the same as the perovskite-forming composition of example IV above, using MAI obtained by a method known in the art [0133] composition II, containing ingredients the same as the perovskite-forming composition of example IV above, but without the addition of CH.sub.3NH.sub.3H.sub.2PO.sub.2, [0134] composition III, containing ingredients the same as the perovskite-forming composition of example IV above , wherein used MAI is the MAI obtained by the method according to the present disclosure and with the addition of CH.sub.3NH.sub.3H.sub.2PO.sub.2).
[0135] Next, a substrate was prepared for the application of the composition of: I, II and III accordingly, as follows: plates were cut out of the PET/ITO (ethylene terephthalate/indium tin oxide) board by means of a laboratory punch and then, by immersion, etched in a 15% hydrochloric acid (HCI) solution to obtain the desired pattern in the ITO conductive layer, The etched plates were cleaned in an ultrasonic bath (cleaning solutions used: deionized water, isopropyl alcohol). The substrates thus prepared were air-dried for 1 hour at 95° C., and then PEDOT:PSS (poly(3,4-ethylene-1,4-dioxyethiophene:styrene polysulphonate) was applied on cleaned and dried substrates using the method of spin-coating in air. Substrates were then heated for 45 minutes at 95° C. in air. Respective perovskite-forming compositions: composition I, composition II, composition III were then applied on the respective plates using the spin-coating technique under nitrogen atmosphere (inside the glove chamber). In order to crystallize the perovskite material, the substrate coated with films of respective perovskite-forming compositions: composition I, composition II, composition III, were heated at 96° C. for 15 minutes.
[0136] The resulting perovskite coatings, in the form of thin films, on PEDOT/PET/ITO substrates, were then viewed under scanning electron microscope (SEM), and images were taken that are presented in
[0137] The results of the SEM analysis of perovskite coatings prepared with compositions I, II and III confirmed the improved morphology of perovskite coatings prepared with MAI obtained using the method according to the present disclosure.
[0138] As shown in the photograph in
[0139] The perovskite layer of
[0140] Now, the layer of
[0141] The resulting coatings were also analysed using X-ray diffraction tests, with the diffractograms obtained presented in
[0142] The thickness measured using an optical profilometer was the same for all the coatings obtained with the compositions: I, II and III, so the differences in intensity of peaks in diffractograms were not due to the amounts of perovskite material varying between samples. The obtained X-ray diffractograms demonstrated, for the samples with the MAI prepared according to the present disclosure (composition II and III), a higher intensity of peaks corresponding to perovskite reflections positions, especially the peak at 14° corresponding to the reflection (110) in the tetragonal symmetry of the perovskite material (
EXAMPLE VI
Preparation of Perovskite Photovoltaic Cells Using MAI
[0143] In order to produce photovoltaic cells with a photoactive perovskite layer, perovskite compositions were prepared with the composition as in example V above, namely: [0144] composition I, containing ingredients as the perovskite-forming composition of example IV above, using MAI obtained using a method known in the art, [0145] composition II, containing ingredients as the perovskite-forming composition of example IV above, containing the MAI according to the present disclosure (with HI produced in situ) but with no CH.sub.3NH.sub.3H.sub.2PO2 added, [0146] composition III, containing ingredients as the perovskite-forming composition is of example IV above, wherein used MAI is the MAI obtained by the method according to the present disclosure, and with the addition of CH.sub.3NH.sub.3H.sub.2PO.sub.2).
[0147] The above compositions were used to prepare photovoltaic cells with a simple sandwich architecture containing the following layers: PET/ITO/PEDOT:PSS/ perovskite: CH.sub.3NH.sub.3PbI.sub.3/PCBM/BCP/Ag.
[0148] For this purpose, substrates containing respective layers of PET/ITO/ PEDOT:PSS/perovskite: CH.sub.3NH.sub.3PbI.sub.3 were prepared for each cell separately from the above perovskite-forming compositions: I, II and III.
[0149] PCBM (phenyl-C61-butyric acid methyl ester) solution dissolved in anhydrous chlorobenzene at a concentration 20 mg/mL was deposited on the perovskite layer of each cell using the spin-coating method under nitrogen (inside glove chamber) immediately after the perovskite layer was obtained. For each cell, the PCBM layer after deposition was heated for 10 minutes at 60° C.
[0150] 5 nm BPC (bathocuproine) and 90 nm silver (Ag) layers were then sequentially thermally vapour-deposited one by one at a predetermined pressure of 1.Math.10.sup.−6 mbar. The characteristics of the obtained cells are presented in
[0151]
[0152] In addition, during the course of the work it was found that the cells with the perovskite layer made of compositions II and III exhibit improved reproducibility and long-term stability of operation compared to the cells with the perovskite layer made of composition I containing prior art MAI, which is due to the difference in the density of defects of the perovskite layer made of the respective composition: I, II, III.
[0153] Furthermore, ageing tests were carried out for selected cells: ageing at the maximum power point with continuous sunlight of 800 W/m.sup.2 in an inert atmosphere and at a temperature of 32° C. The results of these tests, summarized in
EXAMPLE VII
Preparation of a Perovskite-Forming Composition Using FAI
[0154] The perovskite-forming composition was prepared by dissolving the following compounds in the mixture of 400 μL dimethylformamide (DMF) and 100 μof dimethyl sulphoxide (DMSO): [0155] 95.01 mg of formamidinium iodide (FAI) prepared according to the procedure of Example III above, [0156] 38.53 mg of methylammonium bromide CH.sub.3NH.sub.3Br, [0157] 274 mg of lead (II) iodide PbI.sub.2 [0158] a solution of caesium iodide (CsI) in toluene at concentration of 2M.
[0159] The ingredients were mixed for 12 hours, after which the resulting colloidal solution was filtered using a 0.45 μM filter to obtain a colloid with a suitable particle size of the dispersed phase.
[0160] The resulting composition had the form of a stable colloid. No changes in colloidal particle sizes and no agglomeration tendency have been observed (which is the case for colloids containing prior art FAI). During several weeks of observation, the composition had the form of a clear (translucent) colloidal solution.
[0161] Thus, the perovskite-forming composition prepared in the form of a colloidal solution contains the inventive FAI as one of the perovskite-forming ingredients (perovskite precursors).
EXAMPLE VIII
Preparation of Perovskite Coatings Using FAI
[0162] Two perovskite-forming compositions were prepared as follows: [0163] composition I, containing ingredients the same as the perovskite-forming composition of Example VII above, but using FAI obtained by a method known in the art, [0164] composition II containing ingredients the same as the perovskite-forming composition of Example VII above but containing the FAI prepared by the method according to the present disclosure.
[0165] The substrate was then prepared for depositing compositions I and II as described in Example V above. A layer of PTAA (poly[bis(4-phenyl)(2,4,6-trimethylphenyl)amine]) in toluene was then applied onto the plates by spin-coating a PTAA solution in toluene (concentration of 2 mg/mL, solution filtered using a 0.2 μm filter). Composition I (control) and composition II, respectively, were then applied on the substrates using the spin-coating technique, under nitrogen, with the following predetermined parameters: spinning time: 30 seconds, acceleration: 2500 rpm, rotational speed: 2500 rpm. During the last, 8.sup.th second of coating, ethyl acetate (as an anti-solvent) in the amount of 1000 μL pereach plate was added dropwise onto the films being prepared, The films were then heated at 100° C. for 40 minutes to obtain perovskite structures.
[0166] The resulting perovskite coatings, in a form of thin films, on substrates, were then viewed under scanning electron microscope (SEM), and images were taken that are presented in
[0167] The results of the SEM analysis conducted of perovskite coatings prepared with compositions I, II confirmed good morphology of perovskite coatings prepared with FAI obtained using the developed method. The images show larger grains of perovskite material obtained from the inventive FAI compared to the perovskites prepared with prior art FAI.
[0168] The resulting coatings were also analysed using X-ray diffraction tests, with the diffractograms obtained presented in
[0169] The thickness measured using an optical profilometer, was the same for all the coatings obtained with the compositions: I and II, so the differences in intensity of peaks in diffractograms were not caused by different amounts of perovskite material varying between samples. The obtained X-ray diffractograms demonstrated, for the samples with the FAI according to the present disclosure (composition II) a higher intensity of peaks corresponding to perovskite reflections positions, especially (100) in the cubic perovskite phase (
EXAMPLE IX
Preparation of Perovskite Photovoltaic Cells Using FAI
[0170] In order to produce photovoltaic cells with a photoactive layer of perovskite, perovskite compositions were prepared with the ingredients as in example VIII above, containing the FAI according to the present disclosure (composition II—with HI prepared in situ).
[0171] The composition as above was used to prepare a photovoltaic cell with a simple sandwich architecture containing the following layers: PET/ITO/PTAA/perovskite: Cs.sub.0,1(FA.sub.0,83MA.sub.0,17).sub.0,9Pb(I.sub.0,84Br.sub.0,16).sub.3/PCBM/BCP/Ag.
[0172] For this purpose, a substrate containing respective layers of PET/ITO/PTAA/ perovskite were prepared: Cs.sub.0,1(FA.sub.0,83MA.sub.0,17).sub.0,9Pb(I.sub.0,84Br.sub.0,16).sub.3.
[0173] The respective PCBM, BCP and Ag layers were then applied using the same method as described in Example VI above.