LU505007B1 - Synthesis method and application of 4',4''(5'')-di-tert-butyl dicyclohexylo-18-crown ether-6 - Google Patents

Synthesis method and application of 4',4''(5'')-di-tert-butyl dicyclohexylo-18-crown ether-6 Download PDF

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LU505007B1
LU505007B1 LU505007A LU505007A LU505007B1 LU 505007 B1 LU505007 B1 LU 505007B1 LU 505007 A LU505007 A LU 505007A LU 505007 A LU505007 A LU 505007A LU 505007 B1 LU505007 B1 LU 505007B1
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tert
catalyst
synthesis method
diethylene glycol
crown ether
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LU505007A
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German (de)
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Shiquan Cao
Jing Wang
Shan Zhu
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Yan Minhao
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/26Treatment or purification of solutions, e.g. obtained by leaching by liquid-liquid extraction using organic compounds
    • C22B3/302Ethers or epoxides
    • C22B3/304Crown ethers
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D323/00Heterocyclic compounds containing more than two oxygen atoms as the only ring hetero atoms
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B26/00Obtaining alkali, alkaline earth metals or magnesium
    • C22B26/20Obtaining alkaline earth metals or magnesium

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Abstract

The invention discloses a synthesis method and application of 4',4''(5'')- di-tert-butyldicyclohexylo-18-crown ether-6, and belongs to the technical field of strontium extractant synthesis. The synthesis method comprises the following steps: dissolving diethylene glycol in an inert atmosphere, adding a catalyst, preheating and stirring until the catalyst is uniformly dispersed, heating up, adding 3-tert-butyl-7-oxabicyclo [4.1.0] heptane and diethylene glycol bis (p-toluenesulfonate), and obtaining 4',4''(5')-di-tert-butyl dicyclohexyl after the reaction is completed. By changing the synthesis reaction path and optimizing the synthesis reaction parameters, the invention overcomes the problems of hydrogenation danger and difficult purification in the synthesis reaction of DtBuCH18C6.

Description

DESCRIPTION LU505007
SYNTHESIS METHOD AND APPLICATION OF
4',4"(S"")-DI-TERT-BUTYL DICYCLOHEXYLO-18-CROWN ETHER-6
TECHNICAL FIELD
The invention relates to the technical field of synthesis of strontium extractant, in particular to a synthesis method and application of 4',4'(5")-di-tert-butyl dicyclohexylo -18-crown ether-6.
BACKGROUND
With the continuous improvement of nuclear science and technology at home and abroad, the number of nuclear power plants and reactors is increasing, and these nuclear power plants and reactors will produce a large amount of radioactive waste during operation. ’Sr is one of the fission products of >*U and ?‘’Pu in the reactor, and it is a highly toxic nuclide with a half-life of 28.9 years, with high heat release and strong heat release. Separation of “Sr can change High
Level Liquid Waste (HLLW) into medium-low level liquid waste, which is convenient for shallow formation disposal after cement solidification, and it is of positive significance for establishing advanced nuclear fuel cycle. In addition, *°Sr is a radioactive tracer widely used in medical radiotherapy and agriculture. If it can be separated from high-level radioactive waste liquid by effective means, it will have great economic and social effects.
The main methods for separating strontium at home and abroad are chemical precipitation, ion exchange and solvent extraction. Chemical precipitation method is to select a chemical reagent to react with Sr”’ in solution to generate insoluble or insoluble compounds, and then separate them. However, this method has some disadvantages, such as easy to block the pipeline and cause secondary pollution, complicated steps are not conducive to continuous treatment, and solid-liquid separation is difficult under strong radioactive conditions, so it has been rarely used at present. Ion exchange method is a reversible chemical reaction between ion exchanger and ions in liquid phase. Among them, organic ion exchange resin is easy to be damaged under high temperature or high radiation conditions, which reduces the adsorption capacity of metal ions and is not suitable for industrial extraction. Although inorganic ion exchangers such as zeolité/505007 and insoluble multivalent phosphate have the advantages of high temperature resistance and radiation resistance, their development is limited by their low exchange capacity and poor hydraulic properties. The law of solvent extraction is to use the different solubility of substances in two phases to transfer the extracted substance from one liquid phase to another with the help of extractant. This method is convenient for industrialization, because it has the characteristics of simple operation, low requirements for equipment and instruments, and is suitable for the treatment of a large number of high-level liquid waste, and is now widely used in post-treatment processes.
Crown ether is a kind of substance with cyclic structure, which has good selective complexing ability for alkali metal and alkaline earth metal cations. It can be widely used as an extractant in solvent extraction to quickly analyze and separate ’Sr in high-level radioactive waste liquid. 18 crown ether 6 (18-Crown-6, 18C6) and its derivatives have pore sizes that match the ionic radius of Sr”*, and can form stable complexes when interacting with each other, and they have good radiation resistance and hydrolysis stability, so they are the most important extractant in the research of removing ’Sr from high-level radioactive waste liquid. The extraction selectivity of 18C6 for Sr”” is good, but it is very soluble in water, so it is not suitable for use as an extractant. Dicyclohexyl -18- crown-6 (DCH18C6) with good hydrophobicity can be synthesized by grafting alkyl groups on the ring, but when it is dissolved in the organic phase, some of it still enters the water phase, which affects the extraction efficiency. In order to improve its lipophilicity, two tert-butyl groups were grafted to obtain 4',4"(S")-di-tert-butyl dicyclohexo-18-crown ether-6(4', 4" (5")-di-tert-butyl xantho-18-crown-6, DTBuch. The improved crown ether has high hydrophobicity and good lipophilicity, and can achieve high strontium extraction efficiency. It can be used as strontium extractant in SREX process and
CEEX-SREX process.
At present, the main route for the synthesis of DtBuCH18C6 is to synthesize di-tert-butyl dibenzo-18-crown ether-6 first, and then get the final product by hydrogenation. The specific method is to add dibenzo-18-crown-6(DB18C6) dissolved in dichloromethane into excess polyphosphoric acid (PPA) medium, then add excess tert-butanol, react at 60-70°C for a long)505007 time to separate, and then hydrogenate under high pressure to obtain the final product. However, the raw materials and products of this method are mostly flammable and combustible substances, and the hydrogenation conditions at high temperature and high pressure are very dangerous, which is not conducive to large-scale production.
SUMMARY
The invention aims to provide a synthesis method and application of 4, 4 (S")-di-tert-butyldicyclohexylo-18-crown ether-6. The synthesis method is a non-hydrogenation synthesis method, and diethylene glycol, diethylene glycol bis (p-toluenesulfonate) and 3-tert-butyl-7-oxabicyclo [4.1.0] heptane are used as raw materials. By changing the synthesis reaction path and optimizing the synthesis reaction parameters, the problems of hydrogenation danger and difficulty in purification in DtBuCH18C6 synthesis reaction are overcome, and the synthesis of high-purity products is realized, thus providing a brand-new synthesis method of strontium extractant.
In order to achieve the above purpose, the present invention provides the following technical scheme:
One of the technical scheme of the invention is to provide a synthetic method of 4',4"(5")-di-tert-butyldicyclohexylo-18-crown ether-6, comprising: (1) dissolving diethylene glycol in an inert atmosphere; (2) adding catalyst, preheating and stirring until the catalyst is uniformly dispersed, heating, adding 3-tert-butyl-7-oxabicyclo [4.1.0] heptane and stirring; (3) adding catalyst, stirring until the catalyst is uniformly dispersed, adding diethylene glycol bis (p-toluenesulfonate), stirring at room temperature, and obtaining 4' 4'(5")-di-tert-butyldicyclohexylo-18-crown ether-6 after the reaction is completed.
Optionally, the synthetic method of 4'4"(5")-di-tert-butyldicyclohexylo-18-crown ether-6, comprising: (1) dissolving diethylene glycol in an inert atmosphere;
(2) adding catalyst, preheating and stirring until the catalyst is uniformly dispersed, heatink{505007 adding 3- tert-butyl -7- oxabicyclo [4.1.0] heptane and stirring; (3) adding a catalyst, stirring until the catalyst is uniformly dispersed, adding diethylene glycol bis (p-toluenesulfonate), stirring at room temperature, and obtaining 4' 4'(5")-di-tert-butyldicyclohexylo-18-crown ether-6 after the reaction is completed; (4) repeating step (3) for one or more times.
Optionally, the whole reaction is carried out in dimethyl sulfoxide system.
Optionally, the catalyst is sodium hydride.
Optionally, the molar ratio of diethylene glycol and diethylene glycol bis (p-toluenesulfonate) to the total amount of catalyst and 3-tert-butyl-7-oxabicyclo [4.1.0] heptane is 0.9-1.1:0.9-1.1:4 2-4 5:18 -2.2.
Optionally, the molar ratio of diethylene glycol and diethylene glycol bis (p-toluenesulfonate) to the total amount of catalyst and 3-tert-butyl-7-oxabicyclo [4.1.0] heptane 1s1.0:1.0:4.4:2.0.
Optionally, the preheating temperature is 70-90°C; the temperature is raise to 175-195C; the reaction time is 42-45 h.
Optionally, the preheating temperature is 70-90°C; the temperature is raise to 175-195C; the reaction time is 43 h.
Optionally, the inert atmosphere is nitrogen atmosphere.
Optionally, further comprising purification after completing the reaction, including: washing with deionized water, extraction, drying, vacuum evaporation, recrystallization with ether to obtain a crude product, and recrystallization and purification of the crude product with methanol to obtain purified 4',4"(5")-di-tert-butyldicyclohexylo-18-crown ether-6.
The second technical scheme of that invention is to provide a method for extracting strontum from a solution = containing strontium, = comprising: dissolving 4' 4'(5")-di-tert-butyldicyclohexylo-18-crown-6 synthesized by the synthesis method according to any one of claims 1 to 8 with n-octanol, adding into the solution containing strontium, oscillating and extracting, separating the organic phase, and removing the n-octanol.
The beneficial technical effects of the invention are as follows.
According to the invention, diethylene glycol, diethylene glycol bis (p-toluenesulfonate}505007 and 3-tert-butyl-7-oxabicyclo [4.1.0] heptane are used as raw materials, and by changing the synthesis reaction path and optimizing the synthesis reaction parameters, the problems of hydrogenation danger and difficult purification in the synthesis reaction of DtBuCH18C6 are overcome, the synthesis of high-purity products is realized, and a brand-new synthesis method of strontium extractant is provided.
When the synthesized DtBuCH18C6 is used as an extractant to extract strontium, n-octanol as a diluent has the best extraction efficiency. In addition, in this extraction system, the extraction efficiency of strontium is related to the concentration of extractant and nitric acid in water phase, and the time required for equilibrium reaction is short.
BRIEF DESCRIPTION OF THE FIGURES
Fig. 1 1s a synthesis roadmap of Embodiment 1 of the present invention.
Fig. 2 is a one-dimensional NMR spectrum of DtBuCH18C6 prepared in Embodiment 1.
Fig. 3 1s the Fourier infrared spectrum of DtBuCH18C6 prepared in Embodiment 1.
Fig. 4 is the Raman spectrum of DtBuCH18C6 prepared in Embodiment 1.
Fig. 5 is a high-resolution mass spectrum of DtBuCH18C6 prepared in Embodiment 1.
Fig. 6 is a gas chromatogram of DtBuCH18C6 prepared in Embodiment 1.
Fig. 7 shows the extraction efficiency of different concentrations of DtBuCHI8C6 in
Embodiment 2.
Fig. 8 shows the extraction efficiency of different nitric acid concentrations in Embodiment 2.
Fig. 9 is a graph showing the extraction efficiency of different phases in Embodiment 2.
Fig. 10 is an extraction efficiency diagram of different extraction times in Embodiment 2.
DESCRIPTION OF THE INVENTION
A number of exemplary embodiments of the present invention will now be described in detail, and this detailed description should not be considered as a limitation of the present invention, but should be understood as a more detailed description of certain aspects,
characteristics and embodiments of the present invention. It should be understood that th&/505007 terminology described in the present invention is only for describing specific embodiments and is not used to limit the present invention.
In addition, for the numerical range in the present invention, it should be understood that each intermediate value between the upper limit and the lower limit of the range is also specifically disclosed. Intermediate values within any stated value or stated range, as well as each smaller range between any other stated value or intermediate values within the stated range are also included in the present invention. The upper and lower limits of these smaller ranges can be independently included or excluded from the range.
Unless otherwise specified, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention relates. Although the present invention only describes the preferred methods and materials, any methods and materials similar or equivalent to those described herein can also be used in the practice or testing of the present invention.
The terms "comprising", "including", "having" and "containing" used in this article are all open terms, which means including but not limited to.
DtBuCH18C6 standard used in the embodiment of the invention is purchased from
Sigma-Aldrich;
The reagents used in the embodiment of the invention are all commercially available analytical pure, and the experimental water is self-made ultrapure water.
The concentration of Sr”* in the Sr”* standard solution used in the embodiment of the invention is 1000 ug/mL, and the medium is 1.0 mol/L nitric acid.
Embodiment 1
Synthesis of DtBuCH18C6; (1) Under the protection of nitrogen, 5.06 g of sodium hydride is added to 10.70 g of diethylene glycol, and the reaction mixture is heated at 80°C until a solution is obtained. The temperature is raised to 184°C, and 30.85 g of 3-tert-butyl-7- oxabicyclo [4.1.0] heptane is added dropwise. The mixture is stirred at 184°C for 3 h and cooled to room temperature. After addingla)505007 proper amount of CH.Cl,, the solution was washed with brine, dried with MgSO4 and evaporated in vacuum to obtain an intermediate crude product; (2) Under the protection of nitrogen, add 20.72 g of crude intermediate product in step (1) into 18.20 g of 60% nah DMSO suspension, stir for 0.5 h, then add 41.45 g of diethylene glycol bis (p-toluenesulfonate), stir the mixture at room temperature for 40 h, wash it with deionized water, and extract it with ether for three times. The combined extracts are washed with brine, dried with MgSO4 and evaporated in vacuum. The crude product is obtained by recrystallization with ether, and then purified by recrystallization with methanol to obtain white viscous crystals.
The product is 7.57 g with a yield of 31.25%.
The synthesis roadmap of Embodiment 1 is shown in Fig. 1.
DtBuCH18C6 prepared in Embodiment 1 is characterized as follows.
One-dimensional NMR hydrogen spectrum of DtBuCH18C6 is shown in Fig. 2. From Fig. 2, it can be seen that four H's with chemical shifts of 3.94-3.77 belong to four H's on No.4, No.5,
No.16 and No.17 carbons (actually, No.4 C and No.5 carbons here are not completely symmetrical, but the influence of oxygen atoms on them is far greater than that of tert-butyl, and the oxygen atoms near them have the same influence on them. Sixteen H's with chemical shifts of 3.75-3.20 belong to 16 hydrogens on carbon 8, 11, 13, 14, 10, 25, 23 and 24. Four H's with chemical shifts of 2.02-1.72 belong to four hydrogens on carbon 6, 21, 3 and 18 (There are actually eight hydrogens here, but because these carbons are far away from oxygen atoms, the chemical environment changes slightly due to the influence of tert-butyl, and the other four hydrogens will move to high fields). The 10 H's with chemical shifts of 1.50-1.03 belong to the
H's on carbon 21, 6, 3, 1, 20, 18, 19 and 2. The 18 H's with chemical shifts of 0.84-0.82 belong to the 18 H's on carbon 32, 33, 34, 28, 29 and 30. 'HNMR (600MHz, CDCl3):63.94-3.77 (m, 4H), 83.75-3.20 (m, 16H), 82.02-1.72 (m, 4H), §1.50-1.03 (m, 10H), 50.84-0.82 (d, J = 12.0Hz 18H).
The Fourier infrared spectrum of DtBuCH18C6 is shown in Fig. 3. From Fig. 3, it can b&J505007 seen that the peaks of 2925 and 2856 cm” belong to the antisymmetric stretching vibration and symmetric stretching vibration peaks of C-H bond in methyl and methylene respectively. The peaks at 1460 and 1370 cm“ are the bending vibration peaks of C-H bond in methyl and methylene. The peaks of 1243, 1178 and 1082 em” are C-O bond stretching vibration peaks; The peak of 720 cm”! is the out-of-plane rocking vibration of C-H bond in long-chain hydrocarbon group. The peak of 1651 cm”! is H-O-H deformation vibration peak, which may be caused by crown ether absorbing a small amount of water. Because the sample prepared by the invention 1s an oily solid, it is dissolved with n-octanol before infrared detection, so the broad peak with wave number of 3374 cm” is the stretching vibration peak of hydroxyl -OH in n-octanol.
The Raman spectrum of DtBuCH18C6 is shown in Fig. 4. From Fig. 4, it can be seen that the weaker peak with the wave number of 973 cm”! is the C-O bond stretching vibration peak; the peak of 2413 cm”! is the CO; absorption peak in the background. The peak of 2929 cm”! is the stretching vibration peak of C-H bond in methyl or methylene; the peak of 3076 cm”! is the bending vibration peak of C-H bond; the peak of 3593 cm” is the stretching vibration peak of hydroxyl -OH.
The high-resolution mass spectrum of DtBuCH18C6 is shown in Fig. 5. As can be seen from Fig. 5, the chemical formula of DtBuCH18C6 is C28H5206, and its theoretical molecular weight after adding sodium is 507.3662, while its actual molecular weight after adding sodium is 507.3657, with a deviation of 0.0005. The analysis shows that the substance is DtBuCH18C6.
See Fig. 6 for the gas chromatogram of DtBuCH18C6. In Fig. 6, DtBuCH18C6(1) is the gas chromatogram of the standard and DtBuCH18C6(2) is the gas chromatogram of the sample.
From Fig. 6, it can be seen that the broad peak with retention time of 2.5-3.3 min is the solvent peak, the peak with retention time of 4.6-4.9 min is the characteristic peak of the sample, and the retention time of the sample is the same as that of the standard, which indicates that the synthesized substance is DtBuCH18C6.
Embodiment 2
The method of extracting strontium from strontium-containing solution by DtBuCH181&J505007 prepared in Embodiment 1 is investigated as follows.
Use a calibrated glass tube with a stopper to grind at room temperature, and seal the nozzle with a sealing film when oscillating. Adding DtBuCH18C6, diluent and Sr** solution, shaking for 5 min, standing for 30 min, and keeping the water phase. The concentration of strontium in water phase was measured by ICP-OES, and the concentration of strontium in organic phase is obtained by difference subtraction, and the distribution ratio D(Sr) and extraction efficiency E(Sr) are calculated. During the extraction process, the initial concentration of solution Sr** is 10 mg/L, which is obtained by diluting the standard solution of Sr>* by 100 times. (1) DtBuCH18C6 is used as extractant to extract strontium-containing solution, and the effects of n-octanol, sec-octanol, 1,2-dichloroethane, carbon tetrachloride and n-hexane as diluents on strontium extraction were investigated respectively. See Table 1 for the extraction of strontium by each diluent.
Table 1 Effect of DTBUCH 18C6 on Strontium Extraction with Different Organic Solvents as Diluents
DtBuCH18C6
Diluent c(DiBu ; ) D(Sr) | E(SD% (mol:L”)
N-octyl alcohol 18.05 | 9475
Carbon ; 0.1 2.91 74.42 tetrachloride 1,2- i 0.1 3.59 78.20
Dichloroethane
As can be seen from Table 1, under the conditions that the water phase is 10 mg/L strontium solution, the ratio 1s 1:1, the extraction time is 5 min, the concentration of nitric acid is 7 mol/L, and DtBuCH18C6- n-octanol is 0.1 mol/L, among these organic solvents selected in the experiment, n-octanol as diluent and DtBuCH18C6 are mixed into the organic phase, and both the distribution ratio and the extraction rate are the best.
(2) During the experiment, when the fixed water phase is 10 mg/L strontium solution, th&J505007 diluent in the organic phase is n-octanol, the concentration of nitric acid is 7 mol/L, the ratio is 1:1, and the extraction time is 5 min, the effects of the concentration of extractant DtBuCH18C6- n-octanol on strontium extraction are investigated. As can be seen from Fig. 7, E(Sr) increases with the increase of the concentration of DtBuCH18C6, and then decreases. When the concentration is higher than 0.1 mol/L, the extraction rate of strontium changes little, and basically remains above 90%. Therefore, considering the extraction rate, distribution ratio and economic cost, the concentration of DtBuCH18C6 is 0.1 mol/L, which is a more suitable extraction condition. (3) Under the condition that the stationary water phase is 10 mg/L strontium solution and the organic phase is 0.1 mol/L DtBuCH18C6- n-octanol, the ratio is 1:1, and the extraction time is 5 min, the effects of nitric acid concentrations of 1.0, 3.0, 5.0, 7.0 and 9.0 mol/L on strontium extraction are investigated respectively. See Figure 8 for the extraction efficiency of different nitric acid concentrations. As can be seen from Fig. 8, with the increase of acidity, the extraction efficiency of crown ether extraction system first increased and then decreased, and when the concentration of nitric acid in water phase was 7.0 mol/L, the value of E(Sr) reached the maximum. (4) DtBuCH18C6-n-octanol with 10 mg/L strontium solution as the stationary water phase, 7.0 mol/L nitric acid concentration in the water phase and 0.1 mol/L organic phase is extracted for 5 min, and the volume ratio (O/A) of the organic phase to the water phase is 1/3, 1/2, 1/1, 2/1 and 3 respectively. See Fig. 9 for the extraction efficiency of different phases. It can be seen from
Fig. 9 that when the O/A is less than 1, the extraction rate of strontium by crown ether is above 80%. With the increase of water phase, the extraction rate of strontium by crown ether shows a trend of first increasing and then decreasing, and the extraction rate is the highest when the O/A is 1:1, which is 94.75%. (5) DtBuCH18C6- n-octanol with 10 mg/L strontium solution as the stationary water phase, 7.0 mol/L nitric acid concentration in the water phase and 0.1 mol/L organic phase, compared with 1/1, the effects of extraction time for 1, 2, 3, 4, 5, 10 and 30 min on strontium extraction até/505007 shown in Fig. 10. As can be seen from Fig. 10, with the increase of oscillation time, the extraction efficiency E(Sr) of strontium increases slowly at first, and remains basically unchanged after 5 min, which indicates that the extraction of strontium with DtBuCH18C6 as extractant has reached equilibrium in 5 min.
The above-mentioned embodiments only describe the preferred mode of the invention, and do not limit the scope of the invention. Under the premise of not departing from the design spirit of the invention, various modifications and improvements made by ordinary technicians in the field to the technical scheme of the invention shall fall within the protection scope determined by the claims of the invention.

Claims (9)

CLAIMS LU505007
1. A synthetic method of 4',4"(S")-di-tert-butyldicyclohexylo-18-crown ether-6, comprising: (1) dissolving diethylene glycol in an inert atmosphere; (2) adding catalyst, preheating and stirring until the catalyst is uniformly dispersed, heating, adding 3-tert-butyl-7-oxabicyclo [4.1.0] heptane and stirring; (3) adding catalyst, stirring until the catalyst is uniformly dispersed, adding diethylene glycol bis (p-toluenesulfonate), stirring at room temperature, and obtaining 4' 4'(5")-di-tert-butyldicyclohexylo-18-crown ether-6 after completing the reaction.
2. A synthetic method of 4',4"(5")-di-tert-butyldicyclohexylo-18-crown ether-6, comprising: (1) dissolving diethylene glycol in an inert atmosphere; (2) adding catalyst, preheating and stirring until the catalyst is uniformly dispersed, heating, adding 3-tert-butyl-7-oxabicyclo [4.1.0] heptane and stirring; (3) adding catalyst, stirring until the catalyst is uniformly dispersed, adding diethylene glycol bis (p-toluenesulfonate), stirring at room temperature, and obtaining 4' 4'(5")-di-tert-butyldicyclohexylo-18-crown ether-6 after completing the reaction; (4) repeating step (3) for one or more times.
3. The synthesis method according to claim 1, wherein the whole reaction is carried out in dimethyl sulfoxide system.
4. The synthesis method according to claim 1, wherein the catalyst is sodium hydride.
5. The synthesis method according to claim 4, wherein the molar ratio of diethylene glycol and diethylene glycol bis (p-toluenesulfonate) to the total amount of catalyst and 3-tert-butyl-7-oxabicyclo [4.1.0] heptane is 0.9-1.1:0.9-1.1:4.2-4.5:1.8 -2.2.
6. The synthesis method according to claim 1 or 2, wherein the preheating temperature is 70-90°C; the temperature is raise to 175-195°C; the reaction time is 42-45 h.
7. The synthesis method according to claim 1 or 2, wherein the inert atmosphere is nitrogé#/505007 atmosphere.
8. The synthesis method according to claim 1 or 2, further comprising purification after completing the reaction, including: washing with deionized water, extraction, drying, vacuum evaporation, recrystallization with ether to obtain a crude product, and recrystallization and purification of the crude product with methanol to obtain purified 4',4"(5")-di-tert-butyldicyclohexylo-18-crown ether-6.
9. A method for extracting strontium from a solution containing strontium, comprising: dissolving 4',4'(5")-di-tert-butyldicyclohexylo-18-crown-6 synthesized by the synthesis method according to any one of claims 1 to 8 with n-octanol, adding into the solution containing strontium, oscillating and extracting, separating the organic phase, and removing the n-octanol.
LU505007A 2023-08-25 2023-08-25 Synthesis method and application of 4',4''(5'')-di-tert-butyl dicyclohexylo-18-crown ether-6 LU505007B1 (en)

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