Disclosure of Invention
The purpose of the present disclosure is to provide a low-cost method for synthesizing TNU-9 molecular sieve.
In order to achieve the above object, the present disclosure provides a method for synthesizing a TNU-9 molecular sieve, the method comprising the steps of:
a. mixing 1,4-dibromobutane and 1-methylpyrrolidine with a solvent, and carrying out pre-reaction for 0.5-96 h at 15-90 ℃ to obtain a pre-reaction product, wherein the molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent is 1: (1.8-3): (1-20);
b. and c, mixing the pre-reaction product obtained in the step a, inorganic alkali, an aluminum source, a silicon source and water to obtain a mixture to be crystallized, carrying out hydrothermal crystallization treatment on the mixture to be crystallized, and recovering a solid product.
Alternatively, in step a, the molar ratio of the 1,4-dibromobutane, 1-methylpyrrolidine and solvent is 1: (1.9-2.5): (2-18).
Optionally, in step a, the pre-reaction conditions are: the temperature is 15-60 ℃, and the time is 1-48 h.
Optionally, in the step a, the solvent is at least one selected from water, monohydric alcohols of C1-C6, ethers of C4-C6, ketones of C3-C6, polyhydric alcohols of C2-C4 and esters of C3-C6.
Optionally, in step b, the molar composition of the mixture to be crystallized is SiO2:Al2O3:M2O:R:H2O100: (0.5-10): (15-50): (8-20): (800-5000), wherein M2O is an alkali metal oxide, R is the pre-reaction product, and the number of moles of R is calculated by the number of moles of the 1, 4-dibromobutane.
Optionally, in step b, the inorganic base is at least one selected from the group consisting of sodium hydroxide, potassium hydroxide, sodium oxide, potassium oxide, sodium carbonate and potassium carbonate.
Optionally, in step b, the aluminum source is at least one selected from sodium metaaluminate, aluminum nitrate, aluminum sulfate, aluminum isopropoxide and aluminum acetate.
Optionally, in step b, the silicon source is at least one selected from silica gel, silica sol, silica white and ethyl orthosilicate.
Optionally, in step b, the conditions of the hydrothermal crystallization treatment are as follows: the temperature is 140-170 ℃ and the time is 7-14 days.
Optionally, the method further comprises: and after the solid product is recovered, washing, filtering and drying.
According to the technical scheme, the TNU-9 molecular sieve is synthesized by pre-reacting raw materials for synthesizing the template agent for a period of time, then mixing the template agent with other raw materials for synthesizing the molecular sieve according to a certain proportion and carrying out hydrothermal crystallization. The method disclosed by the invention omits the complicated processes of high-cost separation, purification and the like which are necessary for conventionally synthesizing the TNU-9 molecular sieve template agent, avoids a large amount of time consumption, energy consumption and material consumption, and has obvious cost reduction effect; in addition, the defects of incomplete reaction of raw materials and recycling of the raw materials caused by direct mixing and crystallization of the raw materials for synthesizing the template agent and other raw materials for synthesizing the molecular sieve in the prior art are overcome, and waste and ineffective consumption of the reaction raw materials caused by the incomplete reaction are avoided. The TNU-9 molecular sieve synthesized by the method disclosed by the invention has higher crystallinity.
Additional features and advantages of the disclosure will be set forth in the detailed description which follows.
Detailed Description
The following detailed description of specific embodiments of the present disclosure is provided in connection with the accompanying drawings. It should be understood that the detailed description and specific examples, while indicating the present disclosure, are given by way of illustration and explanation only, not limitation.
The present disclosure provides a method for synthesizing a TNU-9 molecular sieve, the method comprising the steps of:
a. mixing 1,4-dibromobutane and 1-methylpyrrolidine with a solvent, and carrying out pre-reaction for 0.5-96 h at 15-90 ℃ to obtain a pre-reaction product, wherein the molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent is 1: (1.8-3): (1-20);
b. and c, mixing the pre-reaction product obtained in the step a, inorganic alkali, an aluminum source, a silicon source and water to obtain a mixture to be crystallized, carrying out hydrothermal crystallization treatment on the mixture to be crystallized, and recovering a solid product.
The TNU-9 molecular sieve is synthesized through pre-reaction of template synthesizing material for some time, mixing the template synthesizing material with other molecular sieve synthesizing material in certain proportion and hydrothermal crystallization. The method disclosed by the invention omits the complicated processes of high-cost separation, purification and the like which are necessary for conventionally synthesizing the TNU-9 molecular sieve template agent, avoids a large amount of time consumption, energy consumption and material consumption, and has obvious cost reduction effect; in addition, the defects of incomplete reaction of raw materials and recycling of the raw materials caused by direct mixing and crystallization of the raw materials for synthesizing the template agent and other raw materials for synthesizing the molecular sieve in the prior art are overcome, and waste and ineffective consumption of the reaction raw materials caused by the incomplete reaction are avoided. The TNU-9 molecular sieve synthesized by the method disclosed by the invention has higher crystallinity.
According to the disclosure, the English name of the 1,4-Dibromobutane is 1,4-Dibromobutane, the CAS number is 110-52-1, and the structural formula is as follows:
according to the present disclosure, the English name of the 1-Methylpyrrolidine is 1-Methylpyrrolidine, the CAS number is 120-94-5, and the structural formula is:
according to the present disclosure, in step a, the molar ratio of the 1,4-dibromobutane, 1-methylpyrrolidine to solvent is preferably 1: (1.9-2.5): (2-18), more preferably 1: (2-2.3): (2-14).
According to the present disclosure, in the step a, the mixing manner of the 1,4-dibromobutane and the 1-methylpyrrolidine and the solvent can be conventional in the art, and preferably, the 1-methylpyrrolidine and the solvent can be mixed first, and then the 1,4-dibromobutane is dropwise added into the obtained mixed solution, wherein the dropwise adding speed can be 1-60 drops/second. The pre-reaction can be carried out in a closed reaction kettle or a reaction kettle with a reflux device. The pre-reaction conditions may preferably be: the temperature is 15-60 ℃, and the time is 1-48 h. The mixing and the pre-reaction may be carried out under stirring in order to obtain the desired effect.
According to the present disclosure, in step a, the solvent may be a common organic solvent and water as long as it is compatible with 1,4-dibromobutane and/or 1-methylpyrrolidine, and for example, the solvent may be at least one selected from water, monohydric alcohols of C1 to C6, ethers of C4 to C6, ketones of C3 to C6, polyhydric alcohols of C2 to C4, and esters of C3 to C6. Preferably, the solvent is at least one selected from water, monohydric alcohols of C1-C4, ethers of C4-C5, ketones of C3-C4, polyhydric alcohols of C2-C3 and esters of C3-C4; specifically, the solvent may be water, methanol, ethanol, diethyl ether, acetone, or the like.
According to the present disclosure, in step b, the pre-reaction product, the inorganic base, the aluminum source, the silicon source and the water may be mixed in a conventional manner in the art, and preferably, the pre-reaction product, the inorganic base and the aluminum source may be dissolved in water to obtain a mixed solution; and then under the condition of stirring, contacting the mixed solution with a silicon source to obtain a mixture to be crystallized. The molar composition of the mixture to be crystallized may be SiO2:Al2O3:M2O:R:H2O100: (0.5-10): (15-50): (8-20): (800-5000), preferably 100: (0.8-8): (20-40): (8-15): (1000 to 4000), wherein M2O is an alkali metal oxide, R is the pre-reaction product, and the number of moles of R is calculated by the number of moles of the 1, 4-dibromobutane.
According to the present disclosure, in step b, the inorganic base, the aluminum source and the silicon source may be conventional species used for synthesizing TNU-9 molecular sieve. For example, the inorganic base may be at least one selected from the group consisting of sodium hydroxide, potassium hydroxide, sodium oxide, potassium oxide, sodium carbonate, and potassium carbonate. The aluminum source may be at least one selected from the group consisting of sodium metaaluminate, aluminum nitrate, aluminum sulfate, aluminum isopropoxide, and aluminum acetate. The silicon source can be at least one selected from silica gel, silica sol, white carbon black and tetraethoxysilane.
According to the disclosure, in step b, the conditions of the hydrothermal crystallization treatment may be: the temperature is 140-170 ℃ and the time is 7-14 days. In order to obtain the desired effect, the hydrothermal crystallization may be performed under stirring.
According to the present disclosure, the method may further comprise: and after the solid product is recovered, washing, filtering and drying. Wherein the washing, filtering and drying are conventional steps for synthesizing the molecular sieve, and the conditions thereof are not particularly limited by the present disclosure. For example, the drying conditions may be: the temperature is 80-120 ℃, and the time is 8-24 h.
The present disclosure is further illustrated by the following examples, but is not limited thereto.
The relative concept and calculation of "relative crystallinity" in the examples and comparative examples is: the sum of the peak areas of the molecular sieve product Z0 synthesized in the comparative example 1 in the range of 21.0-27.5 degrees in the 2 theta interval of an XRD spectrogram is taken as a reference, and the sum is 100 percent; the ratio (in percentage) of the sum of peak areas in the XRD spectrum in the interval of 21.0 to 27.5 ° in 2 θ to the sum of peak areas in the XRD spectrum of Z0 for the products synthesized in the following examples and comparative examples was the relative crystallinity value (r.c.%) of the corresponding products.
In examples and comparative examples, XRD analysis was performed using a Japanese physical D/MAX-IIIA type diffractometer under the following test conditions: cu target, Ka radiation, Ni filter, tube voltage 35kV, tube current 35mA, and scanning range 2 theta 4-55 deg.
In the examples and comparative examples, the specifications and sources of the various reagents used are as follows:
NaOH、Al(NO3)39H2o, absolute ethyl alcohol, methanol, acetone and ether which are all analytically pure and produced in Beijing chemical plants;
1, 4-bis (N-methylpyrrolidine) butane bromide salt (1,4-MPB) aqueous solution with the solid content of 58 weight percent is produced by Guangzhou Daojian refined factory;
1-methylpyrrolidine (1-MP) >98.0 wt%, Tokyo Kasei Kogyo;
1,4-dibromobutane (1,4-DBB) >98.0 wt%, Tokyo chemical industry Co., Ltd;
white carbon black, SiO2Content 97% by weight, Nissan Xinglong Co;
in the examples and comparative examples, the cost estimation method for synthesizing the molecular sieve was: the sum of the prices of all the raw materials for synthesizing the molecular sieve to the weight ratio of the obtained product.
Comparative example 1
This comparative example illustrates the Synthesis of a TNU-9 molecular sieve disclosed in the literature Synthesis, crystalline structure, chromatography, and catalytic properties of TNU-9.Journal of the American Chemical Society,2007,129: 10870-:
9.98g of 1, 4-bis (N-methylpyrrolidine) butane bromide (1,4-MPB) in water was mixed with 2.92g of NaOH, 1.5g of Al (NO)3)3·9H2Dissolving O into a proper amount of deionized water, uniformly mixing, adding 6.19g of white carbon black under the stirring condition to prepare a milky colloidal mixture to be crystallized, wherein the molar composition of the mixture is 4.5(1, 4-MPB): 11Na2O:0.6Al2O3:30SiO2:1200H2And O. The obtained solution was transferred to a crystallization kettle with a polytetrafluoroethylene inner liner of 100ml, and hydrothermal crystallization was carried out for 14 days at 160 ℃ with a rotation speed of 100 rpm. And then stopping the crystallization reaction, washing and filtering the product, and drying the product at the temperature of 80 ℃ for 12 hours to obtain the molecular sieve raw powder Z0.
The XRD measurement of molecular sieve raw powder Z0 was compared with the XRD spectrum of a TNU-9 molecular sieve disclosed in the literature Synthesis, crystalline structure, chromatography, and catalytic properties of TNU-9.Journal of the American Chemical Society,2007,129: 10870-. The relative crystallinity of molecular sieve raw powder Z0 was set to 100% and the synthesis cost was as shown in Table 1.
Comparative example 2
This comparative example is used to illustrate a method for directly synthesizing TNU-9 molecular sieve using precursors for template synthesis, 1-methylpyrrolidine (1-MP) and 1,4-dibromobutane (1,4-DBB), instead of organic template, 1, 4-MPB.
TNU-9 molecular sieves were synthesized according to the procedure of comparative example 1, except that 3.91g of 1-methylpyrrolidine (1-MP) and 3.305g of 1,4-dibromobutane (1,4-DBB) were used instead of 1, 4-bis (N-methylpyrrolidine) butane bromide salt (1,4-MPB), and the molar ratio of 1-methylpyrrolidine to 1,4-dibromobutane was 3: 1. The molecular sieve raw powder Z1 is obtained by synthesis.
XRD testing was performed on the molecular sieve raw powder Z1, and the results were compared with those of the XRD spectrum of TNU-9 molecular sieve disclosed in the literature Synthesis, crystalline structure, chromatography, and catalytic properties of TNU-9.Journal of the American Chemical Society,2007,129:10870-10885, and Z1 was determined to be TNU-9 molecular sieve, and the relative crystallinity and Synthesis cost thereof were calculated and listed in Table 1.
Examples 1-7 are intended to illustrate the process of synthesizing TNU-9 molecular sieves of the present disclosure.
Example 1
29.32g of 1-methylpyrrolidine and 36mL of absolute ethanol are mixed under stirring, 33.05g of 1,4-dibromobutane is dropwise added into the mixed solution at the speed of 5 drops/second, and pre-reaction is carried out for 8 hours at 50 ℃ to obtain a pre-reaction product A1. The molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent ethanol is 1: 2.25: 4.12.
the pre-reaction product A1, 15g Al (NO)3)3·9H2Dissolving O and 29.2g of NaOH solution in a proper amount of deionized water, uniformly mixing, slowly adding 61.9g of white carbon black under the condition of stirring to prepare a milky white colloidal mixture to be crystallized, wherein the molar composition of the milky white colloidal mixture to be crystallized is SiO2:Al2O3:Na2O:A1:H2O100: 2: 36.7: 15: 4000, continuously stirring for 1h, transferring to a 1L high-pressure reaction kettle with mechanical stirring, stirring at 160 ℃ for hydrothermal crystallization for 14 days, stopping the crystallization reaction, washing and filtering the product, and drying at 80 ℃ for 12h to obtain the molecular sieve raw powder B1.
The molecular sieve raw powder B1 is subjected to XRD test, and the spectrum is shown in figure 1. The XRD pattern obtained was compared with that of TNU-9 molecular sieves disclosed in the literature Synthesis, crystalline structure, chromatography, and catalytic properties of TNU-9.Journal of the American Chemical Society,2007,129:10870-10885, to confirm that B1 is a TNU-9 molecular sieve, the relative crystallinity and the Synthesis cost of which are calculated are shown in Table 1.
Example 2
TNU-9 molecular sieve was synthesized according to the procedure of example 1, except that 29.32g of 1-methylpyrrolidine and 43mL of diethyl ether were mixed under stirring, and 33.05g of 1,4-dibromobutane was added dropwise to the above mixture at a rate of 10 drops/sec, and pre-reacted at 35 ℃ for 16 hours to obtain a pre-reaction product A2. The molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent diethyl ether is 1: 2.0: 2.76. the pre-reaction product A2 was used in place of A1 to obtain molecular sieve powder B2, which had an XRD spectrum identical to that of example 1 and whose relative crystallinity and synthesis cost were calculated as shown in Table 1.
Example 3
TNU-9 molecular sieve was synthesized according to example 1, except that 27.37g of 1-methylpyrrolidine was mixed with 35mL of deionized water under stirring, and 33.05g of 1,4-dibromobutane was added dropwise to the above mixture and pre-reacted at 60 ℃ for 48 hours to obtain pre-reaction product A3. The molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent water is 1: 2.1: 12.96. the pre-reaction product A3 was used in place of A1 to obtain molecular sieve powder B3, which had an XRD spectrum identical to that of example 1 and whose relative crystallinity and synthesis cost were calculated as shown in Table 1.
Example 4
TNU-9 molecular sieve was synthesized according to the procedure of example 1, except that 32.58g of 1-methylpyrrolidine was mixed with 160mL of methanol under stirring, and 33.05g of 1,4-dibromobutane was added dropwise to the above mixture at a rate of 30 drops/sec, and pre-reacted at 50 ℃ for 24 hours to obtain a pre-reaction product A4. The molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent methanol is 1: 2.5: 14.5 replacement of A1 by the pre-reaction product A4 gave molecular sieve powder B4 having an XRD pattern in accordance with example 1, the relative crystallinity and synthesis cost of which are calculated and shown in Table 1.
Example 5
TNU-9 molecular sieve was synthesized according to the procedure of example 1, except that 24.76g of 1-methylpyrrolidine was mixed with 155mL of acetone under stirring, and 33.05g of 1,4-dibromobutane was added dropwise to the mixture at a rate of 20 drops/sec, and pre-reacted at 40 ℃ for 4 hours to obtain a pre-reaction product A6. The molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent acetone is 1: 1.9: 14.1. the pre-reaction product A5 was used in place of A1 to obtain molecular sieve powder B5, which had an XRD spectrum identical to that of example 1 and whose relative crystallinity and synthesis cost were calculated as shown in Table 1.
Example 6
TNU-9 molecular sieve was synthesized by the method of example 1 except that a mixture of 160mL of ethanol and 33.05g of 1,4-dibromobutane was added dropwise to 33.89g of 1-methylpyrrolidine at a rate of 40 drops/sec under stirring, and pre-reacted at 50 ℃ for 10 hours to obtain a pre-reaction product A6. The molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent ethanol is 1: 2.6: 18.32. the pre-reaction product A6 was used in place of A1 to obtain molecular sieve powder B5, which had an XRD spectrum identical to that of example 1 and whose relative crystallinity and synthesis cost were calculated as shown in Table 1.
Example 7
TNU-9 molecular sieve was synthesized according to the procedure of example 1, except that 16mL of a mixture of ethanol and 33.05g of 1,4-dibromobutane was added dropwise to 23.46g of 1-methylpyrrolidine at a rate of 3 drops/sec under stirring, and pre-reacted at 75 ℃ for 60 hours to obtain a pre-reaction product A7. The molar ratio of the 1,4-dibromobutane to the 1-methylpyrrolidine to the solvent ethanol is 1: 1.8: 1.83. the pre-reaction product A7 was used in place of A1 to obtain molecular sieve powder B7, which had an XRD spectrum identical to that of example 1 and whose relative crystallinity and synthesis cost were calculated as shown in Table 1.
TABLE 1
As can be seen from Table 1, the method disclosed by the invention can obviously reduce the synthesis cost of the TNU-9 molecular sieve, and the prepared TNU-9 molecular sieve has higher relative crystallinity.
The preferred embodiments of the present disclosure are described in detail with reference to the accompanying drawings, however, the present disclosure is not limited to the specific details of the above embodiments, and various simple modifications may be made to the technical solution of the present disclosure within the technical idea of the present disclosure, and these simple modifications all belong to the protection scope of the present disclosure.
It should be noted that, in the foregoing embodiments, various features described in the above embodiments may be combined in any suitable manner, and in order to avoid unnecessary repetition, various combinations that are possible in the present disclosure are not described again.
In addition, any combination of various embodiments of the present disclosure may be made, and the same should be considered as the disclosure of the present disclosure, as long as it does not depart from the spirit of the present disclosure.