90076-65-6Relevant articles and documents
7Li NMR studies on complexation reactions of lithium ion with cryptand C211 in ionic liquids: Comparison with corresponding reactions in nonaqueous solvents
Shirai, Atsushi,Ikeda, Yasuhisa
, p. 1619 - 1627 (2011)
7Li NMR spectra of DEME-TFSA [DEME = N,N-diethyl-N-methyl-N-(2- methoxyethyl)ammonium; TFSA = bis(trifluoromethanesulfonyl)amide], EMI-TFSA (EMI = 1-ethyl-3-methylimidazolium), MPP-TFSA (MPP = N-methyl-N-propylpyridinium), DEME-PFSA [PFSA = bis(pentafluoroethanesulfonyl)amide], and DEME-HFSA [HFSA = bis(heptafluoropropanesulfonyl)amide] ionic liquid (IL) solutions containing LiX (X = TFSA, PFSA, or HFSA) and C211 (4,7,13,18-tetraoxa-1,10-diazabicyclo[8.5.5] eicosane) were measured at various temperatures. As a result, it was found that the uncomplexed Li(I) species existing as [Li(X)2]- in the present ILs exchange with the complexed Li(I) ([Li?C211]+) and that the exchange reactions proceed through the bimolecular mechanism, [Li?C211]+ + [*Li(X)2]- = [*Li?C211]+ + [Li(X)2]-. Kinetic parameters [ks/(kg m-1 s-1) at 25 °C, ΔH?/(kJ mol-1), ΔS?/ (J K-1 mol-1)] are as follows: 5.57 × 10 -2, 69.8 ± 0.4, and -34.9 ± 1.0 for the DEME-TFSA system; 5.77 × 10-2, 70.6 ± 0.2, and -31.9 ± 0.6 for the EMI-TFSA system, 6.13 × 10-2, 69.0 ± 0.3, and -36.7 ± 0.7 for the MPP-TFSA system; 1.35 × 10-1, 65.2 ± 0.5, and -43.1 ± 1.4 for the DEME-PFSA system; 1.14 × 10-1, 64.4 ± 0.3, and -47.1 ± 0.6 for the DEME-HFSA system. To compare these kinetic data with those in conventional nonaqueous solvents, the exchange reactions of Li(I) between [Li?C211]+ and solvated Li(I) in N,N-dimethylformamide (DMF) and dimethyl sulfoxide (DMSO) were also examined. These Li(I) exchange reactions were found to be independent of the concentrations of the solvated Li(I) and hence proposed to proceed through the dissociative mechanism. Kinetic parameters [ks/s -1 at 25 °C, ΔH?/(kJ mol-1), ΔS?/(J K-1 mol-1)] are as follows: 1.10 × 10-2, 68.9 ± 0.2, and -51.3 ± 0.4 for the DMF system; 1.13 × 10-2, 76.3 ± 0.3, and -26.3 ± 0.8 for the DMSO system. The differences in reactivities between ILs and nonaqueous solvents were proposed to be attributed to those in the chemical forms of the uncomplexed Li(I) species, i.e., the negatively charged species ([Li(X)2]-) in ILs, and the positively charged ones ([Li(solvent)n]+) in nonaqueous solvents.
METHOD FOR PRODUCING PHOSPHORYL IMIDE SALT, METHOD FOR PRODUCING NONAQUEOUS ELECTROLYTE SOLUTION CONTAINING SAID SALT, AND METHOD FOR PRODUCING NONAQUEOUS SECONDARY BATTERY
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Paragraph 0282; 0294, (2020/05/02)
To provide a method for producing a phosphoryl imide salt represented by the following general formula (1) at a satisfactory yield by cation exchange. The method comprises the step of performing cation exchange by bringing a phosphoryl imide salt represented by the following general formula (2) into contact with a cation exchange resin having M1 n+ or a metal salt represented by the general formula (4) in an organic solvent having a water content of 0.3% by mass or less.
New process of bis-trifluoro sulfonimide salt
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Paragraph 0062; 0063; 0066; 0067, (2019/06/12)
The invention provides a preparation method of a bis-trifluoro sulfonimide salt. The method comprises the following steps of S1, preparing corresponding N-alkyl-substituted bis-trifloromethane sulfonimide with primary amine and trifluoromethyl sulfonic anhydride; S2, reacting the N-alkyl-substituted bis-trifloromethane sulfonimide with a salt to obtain a crude product; S3, crystallizing the crudeproduct and then drying the crude product in vacuum to obtain the bis-trifloromethane sulfonimide salt. The method has the advantages that N-alkyl-substituted bis-trifloromethane sulfonimide is stablein property and does not generate corrosive substances in a whole reaction process, three wastes are hardly generated, the method is suitable for large-scale production, the high-purity battery-gradebis-trifloromethane sulfonimide salt can be obtained, and a high implementation value and considerable social and economic benefits are acquired.
A method of preparing lithium imide fluorine sulfuryl
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Paragraph 0048-0049; 0053-0054, (2017/01/19)
The invention relates to a method for preparing fluorine sulfimide lithium and belongs to the field of fine chemical industries. The method comprises the steps as follows: lithium salt and deionized water are prepared into a turbid liquid with the mass concentration of the lithium salt in a range of 20-50% in a reaction still, a refined fluorine sulfimide acid solution is added dropwise to obtain a reaction solution under the condition of stirring, the mass content of the deionized water in the fluorine sulfimide acid solution is in a range of 5-20%, the reaction temperature is in a range of 50-150 DEG C, and the reaction is stopped when the pH value of the reaction solution is in a range of 6-8. Non-vacuum drying is performed on the reaction solution firstly, and when the mass content of the deionized water is lower than or equal to 0.5%, vacuum drying is performed. The method is easy to operate, higher in process safety and capable of effectively improving the purity of products and satisfying requirements of lithium battery industries for the high purity.